Liquid-gas separator

ABSTRACT

A method and system for separating a flow of matter is shown and described. The system includes one or more flow separation devices, one or more surgical instruments, and one or more suction sources. In some embodiments, the flow of matter comprises biological material. In some embodiments, the flow of matter comprises surgical waste.

CROSS REFERENCE

This application is a continuation of U.S. patent application Ser. No.17/157,430 filed on Jan. 25, 2021 (now U.S. patent Ser. No. 11/458,242)which is a divisional of U.S. patent application Ser. No. 16/567,505filed on Sep. 11, 2019 (now U.S. patent Ser. No. 10/905,803) which is acontinuation of U.S. patent application Ser. No. 15/296,894 filed onOct. 18, 2016 (now U.S. patent Ser. No. 10/420,867), which claimspriority to U.S. provisional application 62/243,417, filed on Oct. 19,2015; U.S. provisional application 62/257,214, filed on Nov. 18, 2015;each of which is entirely incorporated herein by reference.

BACKGROUND

Suction products suctioned from a field may comprise mixtures of solids,liquids, and gases.

SUMMARY

Described herein are devices, systems, and methods for suctioning a flowof matter from a field, such as a surgical field.

An aspect of the present disclosure provides a system for separation aflow of matter. The system comprises a flow separation device, asurgical instrument, and a suction source. The flow separation devicecomprises (a) a hollow body comprising a first end, a second end, and aninner volume therebetween; (b) a suction port disposed at the first end;(c) a collection port disposed at the second end; (d) an input portdisposed between the first end and the second end and fluidicallyconnected to the inner volume; (e) one or more baffles disposed withinthe inner volume between the first end and the second end; and (0 ashaft disposed within the inner volume. In some embodiments, the inputport is configured to receive a flow of matter comprising a gas, aliquid, a solid, or combination thereof. In some embodiments, the shaftis configured to direct the flow of matter received into the hollowbody. In some embodiments, at least a portion of a liquid of the flow ofmatter exits the hollow body from a port different than a port fromwhich at least a portion of a gas of the flow of matter exits.

In some embodiments, the shaft directs at least a portion of the flow ofmatter in a cyclonic pattern along an inner surface of the hollow body.In some embodiments, the gas exits the suction port and the liquid exitsthe collection port. In some embodiments, the one or more baffles areconfigured to prevent the flow of matter from passing directly from theinput port to the suction port without first traversing at least aportion of the circumference of the inner surface. In some embodiments,the one or more baffles comprise a plurality of openings configured toreceive at least a portion of the flow of matter. In some embodiments,the plurality of openings is distal to the input port. In someembodiments, the one or more baffles comprise a tapered section orcomprise a plurality of cylindrical sections having different diameters.In some embodiments, the second end comprises a conical shape. In someembodiments, the hollow body comprises a cylindrical shape. In someembodiments, the flow of matter comprises surgical waste. In someembodiments, the flow of matter comprises biological material.

In some embodiments, the input port is proximal to the suction port anddistal from the collection port. In some embodiments, the suction portis configured to couple to the suction source. In some embodiments, thesuction source is a passive suction source. In some embodiments, thecollection port is configured to couple to a collection container. Insome embodiments, the flow separation device is attachable or formedtherein a collection container. In some embodiments, the one or morebaffles aids in the separation of gas, of liquid, or a combinationthereof from the flow of matter.

In some embodiments, the input port forms an angle relative to a centralaxis of the hollow body that is less than 90 degrees. In someembodiments, the angled input port enhances entry of the flow of matterinto the input port, enhances a cyclonic pattern of flow along an innersurface of the hollow body, or a combination thereof.

In some embodiments, the flow separation device enhances a suctioncapacity of the surgical instrument operatively coupled to the inputport. In some embodiments, the suction capacity is increased at leastabout 1.25 fold compared to a surgical instrument not operativelycoupled to the flow separation device.

In some embodiments, the flow separation device is disposable. In someembodiments, the flow separation device further comprises one or morefilters. In some embodiments, the one or more filters are disposedadjacent to the collection port. In some embodiments, a pore size of theone or more filters is less than about 1 micron. In some embodiments,the one or more filters collect one or more solids.

In some embodiments, the one or more solids are a bacterium, a bacterialfragment, a bacterial particle, a virus, a viral fragment, a viralparticle, or any combination thereof. In some embodiments, the flowseparation device further comprises one or more positively chargedmatrices, one or more negatively charged matrices, or any combinationthereof. In some embodiments, the one or more positively chargedmatrices, one or more negatively charged matrices, or any combinationthereof are operatively connected to the suction port. In someembodiments, the flow separation device is operatively coupled to one ormore surgical instruments, one or more suctioning devices, one or moresuction sources, one or more canisters, one or more filtration units,one or more charged matrices, or any combination thereof.

Another aspect of the present disclosure provides a flow separationdevice. In some embodiments, the flow separation device comprises: (a) aseparator body having a cylindrical cavity having a cylindrical wall andfirst cylindrical cavity end and a second cylindrical cavity end,configured to operate with the first cylindrical cavity end up; (b) aconical cavity having a narrow end and a wide end, the wide end mated tothe second cylindrical cavity end; (c) an input port disposed in thecylindrical cavity wall, configured to receive a flow of matter; (d) ansuction port mated to the first cylindrical cavity end and configured tocouple to a vacuum source; (e) an collection port mated to the narrowend of the conical cavity and configured to couple to a waste deposit;(f) a baffle disposed between the input port and the suction port,configured to prevent the flow of matter from passing directly from theinput port to the suction port without first traversing at least aportion of a circumference of an interior of the cylindrical wall; and(g) a cylindrical shaft disposed within a center of the cylindricalcavity and configured to direct the flow of matter within thecylindrical cavity.

In some embodiments, the input port is located off-axis of an axisdefined by the longitudinal center of the separator body. In someembodiments, the input port is located closer to the first cylindricalend than the second cylindrical end. In some embodiments, the suctionsource comprises a vacuum pump.

In some embodiments, the suction source comprises a positive pressureoperated suction generator that utilizes a Coanda effect. In someembodiments, the suction source comprises a positive pressure operatedsuction generator that utilizes a Venturi effect.

In some embodiments, the baffle comprises a plurality of openings toallow passage of the flow of matter, comprising separated portionsthereof, out of the suction port. In some embodiments, the bafflecomprises a solid surface located proximal to the input port and distalto the plurality of openings, configured to prevent the flow of matter,comprising separated portions thereof, from passing directly from theinput port to the suction port without first traversing at least aportion of a circumference of the cylindrical cavity wall.

In some embodiments, the baffle is integral to the cylindrical shaft. Insome embodiments, the cylindrical shaft comprises a plurality of conicsections each comprising a wide end and a narrow end of varyingdiameters and a plurality of cylindrical sections of varying diameterconfigured to direct the flow of matter within the cylindrical cavity.In some embodiments, the separator is further configured to allowpassage of the flow of matter, unseparated, from the input port to thesuction port when the flow of matter is no longer able to be expelledout of the collection port.

Another aspect of the present disclosure provides a method of operatinga separator. In some embodiments, the method comprises: (a) providing aseparator comprising: a separator body comprising: (i) a cylindricalcavity having a cylindrical wall and first cylindrical cavity end and asecond cylindrical cavity end, configured to operate with the firstcylindrical cavity end up; (ii) a conical cavity having a narrow end anda wide end, the wide end mated to the second cylindrical cavity end;(iii) an input port disposed in the cylindrical cavity wall configuredto receive a flow of matter; (iv) an suction port mated to the firstcylindrical cavity end and configured to couple to a vacuum source; (v)a collection port mated to the narrow end of the conical cavity andconfigured to couple to a waste deposit; (vi) a baffle disposed betweenthe input port and the suction port, configured to prevent the flow ofmatter from passing directly from the input port to the suction portwithout first traversing at least a portion of a circumference of aninterior of the cylindrical wall; and (vii) a cylindrical shaft disposedwithin a center of the cylindrical cavity and configured to direct theflow of matter within the cylindrical cavity, (b) attaching the suctionport to the suction source; (c) mating the collection port to a wastedeposit; (d) activating the suction source thereby creating the flow ofmatter into the input port; (e) expelling portions of the flow of matterout of the collection port; and (f) pulling portions of the flow ofmatter out of the suction port.

In some embodiments, the method further comprises locating the inputport off-axis of an axis defined by a longitudinal center of theseparator body. In some embodiments, the method further compriseslocating the input port closer to the first cylindrical end than thesecond cylindrical end. In some embodiments, the method furthercomprises providing the suction source using a vacuum pump.

In some embodiments, the method further comprises providing the suctionsource using a positive pressure operated suction generator thatutilizes a Coanda effect. In some embodiments, the method furthercomprises providing the suction source using a positive pressureoperated suction generator that utilizes a Venturi effect.

In some embodiments, the method further comprises providing the bafflewith a plurality of openings allowing passage of the flow of matter,comprising separated portions thereof, out of the suction port. In someembodiments, the method further comprises providing the baffle a solidsurface located proximal to the input port and distal to the opening,thereby preventing the flow of matter, comprising separated portionsthereof, from passing directly from the input port to the suction portwithout first traversing at least a portion of a circumference of thecylindrical cavity wall.

In some embodiments, the method further comprises integrating the baffleto the cylindrical shaft. In some embodiments, the method furthercomprises providing the cylindrical shaft a plurality of conic sectionseach comprising a wide end and a narrow end of varying diameters and aplurality of cylindrical sections of varying diameter thereby directingthe flow of matter along the cylindrical cavity wall. In someembodiments, the method further comprises allowing passage of the flowof matter, unseparated, from the input port to the suction port when theflow of matter is no longer expelling out of the collection port. Insome embodiments, the method further comprises providing the suctionsource using a vacuum pump. In some embodiments, the method furthercomprises providing the suction source using a positive pressureoperated suction device that utilizes a Coanda effect. In someembodiments, the method further comprises coupling the separator to acanister.

Another aspect of the present disclosure provides a system of flowseparators. In some embodiments, the system of flow separatorscomprises: (a) one or more separators, each comprising: a separator bodycomprising: (i) a cylindrical cavity having a cylindrical wall and firstcylindrical cavity end and a second cylindrical cavity end, configuredto operate with the first cylindrical cavity end up; (ii) a conicalcavity having a narrow end and a wide end, the wide end mated to thesecond cylindrical cavity end; (iii) an input port disposed in thecylindrical cavity wall, configured to receive a flow of matter; ansuction port mated to the first cylindrical cavity end and configured tocouple to a vacuum source; (iv) an collection port mated to the narrowend of the conical cavity and configured to couple to a waste deposit;(v) a baffle disposed between the input port and the suction port,configured to prevent the flow of matter from passing directly from theinput port to the suction port without first traversing at least aportion of a circumference of the interior of the cylindrical wall; and(vi) a cylindrical shaft disposed within the center of the cylindricalcavity and configured to direct the flow within the cylindrical cavity;and (b) one or more canisters configured to couple to an associatedseparator.

In some embodiments, the suction port of one separator is coupled to theinput port of another separator. In some embodiments, the one or moreseparators are configured to discontinue filling a first canister whenthe first canister has reached a pre-determined volume and allow theflow of matter, unseparated, to pass through the input port and out ofthe output port of a first separator to the input port of a secondseparator coupled to a canister that is not filled to a pre-determinedcapacity.

Another aspect of the present disclosure provides a method of operatinga separator system. In some embodiments, the system comprises: (a)providing one or more separators, each comprising: a separator bodycomprising: (i) a cylindrical cavity having a cylindrical wall and firstcylindrical cavity end and a second cylindrical cavity end, configuredto operate with the first cylindrical cavity end up; (ii) a conicalcavity having a narrow end and a wide end, the wide end mated to thesecond cylindrical cavity end; (iii) an input port disposed in thecylindrical cavity wall, configured to receive a flow of matter; (iv) ansuction port mated to the first cylindrical cavity end and configured tocouple to a vacuum source; (v) an collection port mated to the narrowend of the conical cavity and configured to couple to a waste deposit;(vi) a baffle disposed between the input port and the suction port,configured to prevent the flow of matter from passing directly from theinput port to the suction port without first traversing at least aportion of the circumference of the interior of the cylindrical wall;and (vii) a cylindrical shaft disposed within the center of thecylindrical cavity and configured to direct the flow of matter withinthe cylindrical cavity; (b) coupling the suction port of one separatorto the input port of another separator, forming a series of separators;(c) attaching the suction port of a last separator in the series ofseparators to the suction source; (d) activating the suction sourcethereby creating a flow of matter through the series of separators; (e)receiving the flow of matter into the input port of a first separator inthe series of separators; (f) pulling gas out of the suction port of thefirst separator while an associated canister is filled below apre-determined capacity; expelling portions of the flow of matter out ofthe collection port of the first separator until an associated canisteris filled to a pre-determined limit; (g) passing the flow of matter fromthe input port out of the suction port of the first separator to aninput port of a second separator in the series of separators coupled toa canister that is not filled to a predetermined limit; receiving theflow of matter into the input port of the second separator; (h) pullinggas out of the suction port of the second separator while an associatedcanister is filled below a pre-determined capacity; and (i) expellingportions of the flow of matter out of the collection port of the secondseparator until an associated canister is filled to a pre-determinedlimit.

In some embodiments, the method further comprises providing the suctionsource using a vacuum pump. In some embodiments, the method furthercomprises providing the suction source using a positive pressureoperated suction generator that utilizes a Coanda effect.

Another aspect of the present disclosure provides a liquid-gas flowseparator. In some embodiments, the separator comprises: (a) acylindrical cavity comprising a cylindrical cavity wall, a firstcylindrical cavity end, and a second cylindrical cavity end, theseparator configured to operate with the first cylindrical cavity endbeing up; (b) a suction port to be coupled to a suction source, thesuction port being in the first cylindrical cavity end; (c) a conicalcavity, the conical cavity comprising a wide end and a narrow end, thewide end being mated to the second cylindrical cavity end; (d) acollection port at the narrow end of the conical cavity; (e) an inputport to receive a flow of matter comprising a mixture of liquid and gas,the input port being in the cylindrical cavity wall, the flow of matterinduced into the separator by the suction source, the input portconfigured to direct liquids in the flow the matter to cling to thecylindrical cavity wall; (f) a baffle disposed between the input portand the suction port, the baffle configured to prevent liquids in theflow of matter from being pulled directly from the input port to thesuction port without traversing at least a first portion of acircumference of the cylindrical cavity wall, the baffle configured toallow gasses in the flow of matter to separate from the liquids in theflow of matter and be pulled out of the separator via the suction port;and a cylindrical central member disposed within the cylindrical cavity,the central member disposed to form an annular cavity between thecylindrical central member and the cylindrical cavity wall, the liquidsin the flow of matter pass through the annular cavity before droppingout the collection port.

In some embodiments, the flow of matter further comprises solids, thesolids in the flow of matter pass through the annular cavity beforedropping out the collection port. In some embodiments, the bafflecomprises a plurality of openings to allow the gasses in the flow ofmatter to be pulled out of the separator via the suction port. In someembodiments, the baffle comprises a solid portion that prevents liquidsin the flow of matter from being pulled directly from the input port tothe suction port, the solid portion corresponding to at least the firstportion of the circumference.

In some embodiments, the central member comprises a tapered sectiondisposed in the conical cavity. In some embodiments, the central membercomprises a plurality of cylindrical sections comprising differentdiameters.

In some embodiments, a plurality of cylindrical sections includes afirst section that defines a first portion of the annular cavity and asecond section that defines a second portion of the annular cavity. Insome embodiments, the first portion is disposed between the baffle andthe second portion, the second portion is disposed between the firstportion and the conical cavity. In some embodiments, the central memberfurther comprises a tapered section disposed in the conical cavitythereby forming a hollow cone shaped cavity, the hollow cone shapedcavity disposed between the second portion and the second port.

Another aspect of the present disclosure provides a method of operatinga liquid-gas flow separator. In some embodiments, the method comprises:(a) providing a cylindrical cavity having a cylindrical cavity wall, afirst cylindrical cavity end, and a second cylindrical cavity end, andoperating the separator with the first cylindrical cavity end being up;(b) coupling a suction port to a suction source, the suction port beingin the first cylindrical cavity end; (c) providing a conical cavity, theconical cavity having a wide end and a narrow end, and mating the wideend to the second cylindrical cavity end; (d) providing a collectionport at the narrow end of the conical cavity; (e) receiving a flowcomprising a mixture of liquid and gas at a input port, the input portbeing in the cylindrical cavity wall, and inducing the flow into theseparator by the suction source, directing liquids in the flow to clingto the cylindrical cavity wall by configuring the input port; (0providing a baffle disposed between the input port and the suction port,thereby preventing liquids in the flow from being pulled directly fromthe input port to the suction port without traversing at least a firstportion of a circumference of the cylindrical cavity wall, and allowinggasses in the flow to separate from the liquids in the flow and pullingthe gasses out of the separator via the suction port; and (g) providinga cylindrical central member disposed within the cylindrical cavity,disposing the central member to form an annular cavity between thecentral member and the cylindrical cavity wall, and passing the liquidsin the flow through the annular cavity before dropping out thecollection port.

In some embodiments, the method further comprises providing a flowfurther comprising solids and passing the solids in the flow through theannular cavity before dropping out the collection port. In someembodiments, the method further comprises providing the bafflecomprising a plurality of openings to allow the gasses in the flow to bepulled out of the separator via the suction port. In some embodiments,the method further comprises preventing liquids in the flow from beingpulled directly from the input port to the suction port by providing thebaffle comprising a solid portion, the solid portion corresponding to atleast the first portion of the circumference.

In some embodiments, the method further comprises providing the centralmember comprising a tapered section disposed in the conical cavity. Insome embodiments, the method further comprises providing the centralmember comprising a plurality of cylindrical sections comprisingdifferent diameters. In some embodiments, the method further comprisesproviding a plurality of cylindrical sections comprising a first sectiondefining a first portion of the annular cavity and a second sectiondefining a second portion of the annular cavity.

In some embodiments, the method further comprises disposing the firstportion between the baffle and the second portion and disposing thesecond portion between the first portion and the conical cavity. In someembodiments, the method further comprises providing the central member atapered section disposed in the conical cavity thereby forming a hollowcone shaped cavity and disposing the hollow cone shaped cavity betweenthe second portion and the collection port.

Another aspect of the present disclosure provides a flow separator. Insome embodiments, the flow separator comprises: (a) a cylindrical cavitycomprising a cylindrical wall comprising a first end and a second end,the first end disposed in an upward position, and means for directing aflow of matter along a circumference of the cylindrical cavity wall; (b)an input port mated to the cylindrical cavity wall, and means forreceiving the flow of matter and directing the flow of matter into thecylindrical cavity; (c) an suction port mated to the first end of thecylindrical cavity, and means for coupling the separator to a suctionsource; (d) the suction port comprising means for expelling at leastgasses out of the separator; (e) a conical cavity comprising a wide endand a narrow end and a conical cavity wall, the wide end mated to thesecond end of the cylindrical cavity, and a means for directing the flowof matter to create a flow within the cylindrical cavity whereby gassesare directed out of the suction port and at least liquids are directedout of narrow end of the conical cavity; (0 an collection port mated tothe narrow end of the conical cavity, and a means for expelling at leastliquids for collection; (g) a baffle disposed between the input port andthe first end of the cylindrical cavity, and means for preventingliquids and/or solids from passing from the input port to the suctionport without first traversing at least a portion of the circumference ofthe cylindrical cavity wall; and (h) a cylindrical central memberdisposed concentrically within the cylindrical cavity forming an annularcavity between the cylindrical central member and the cylindrical cavitywall to allow passage of at least liquids, and means for expelling atleast liquids out of the collection port for collection.

In some embodiments, the flow of matter comprises one or more ofliquids, solids and gasses, and means for the liquids and/or solids topass through the annular cavity and out of the collection port.

In some embodiments, the baffle comprises a plurality of openings, andmeans for allowing matter to pass through the baffle and out the suctionport after traversing at least a portion of the circumference of thecylindrical cavity wall. In some embodiments, the baffle comprises asolid portion disposed proximally to the input port, and means forpreventing liquids and/or solids in the flow of matter from being pulleddirectly from the input port to the suction port before traversing atleast a portion of a circumference of the cylindrical cavity wall.

In some embodiments, the central member comprises a tapered sectiondisposed in the conical cavity, and means for directing the flow ofmatter within the separator. In some embodiments, the central membercomprises a plurality of cylindrical sections comprising differentdiameters, and means for directing the flow of matter within theseparator.

In some embodiments, a plurality of cylindrical sections include a firstsection that defines a first portion of the annular cavity and a secondsection that defines a second portion of the annular cavity, and meansfor directing the flow of matter within the separator. In someembodiments, the first portion is disposed between the baffle and thesecond portion, the second portion is disposed between the first portionand the conical cavity, and means for directing the flow of matterwithin the separator. In some embodiments, the central member furthercomprises a tapered section disposed in the conical cavity therebyforming a hollow cone shaped cavity, the hollow cone shaped cavitydisposed between the second portion and the collection port, and meansfor directing the flow of matter through the hollow cone shaped cavity.

Another aspect of the present disclosure provides a system of liquid-gasseparators. In some embodiments, the system comprises: (a) one or moreseparators comprising: (i) a cylindrical cavity comprising a cylindricalwall comprising a first end and a second end, the first end disposed inan upward position, and means for directing a flow of matter along thecircumference of the cylindrical cavity wall; (ii) an input port matedto the cylindrical cavity wall, and means for receiving the flow ofmatter and directing the flow of matter into the cylindrical cavity;(iii) an suction port mated to the first end of the cylindrical cavity,and means for coupling the separator to a suction source; (iv) thesuction port comprising means for expelling at least gasses out of theseparator; (v) a conical cavity comprising a wide end and a narrow endand a conical cavity wall, the wide end mated to the second end of thecylindrical cavity, and a means for directing the flow of matter tocreate a flow within the cylindrical cavity whereby gasses are directedout of the suction port and at least liquids are directed out of narrowend of the conical cavity; (vi) an collection port mated to the narrowend of the conical cavity, and a means for expelling at least liquidsfor collection; (vii) a baffle disposed between the input port and thefirst end of the cylindrical cavity, and means for preventing liquidsand/or solids from passing from the input port to the suction portwithout first traversing at least a portion of the circumference of thecylindrical cavity wall; and (viii) a cylindrical central memberdisposed concentrically within the cylindrical cavity forming an annularcavity between the cylindrical central member and the cylindrical cavitywall to allow passage of at least liquids, and means for expelling atleast liquids out of the collection port for collection; (b) one or morecanisters each mated to a corresponding separator, and a means forcoupling to the separator and collecting at least a portion of the flowof matter from the collection port; and (c) a suction source, and ameans for providing suction to the suction port.

In some embodiments, the flow of matter comprises one or more ofliquids, solids and gasses, and means for the liquids and/or solids topass through the annular cavity and out of the collection port. In someembodiments, the baffle comprises a plurality of openings, and means forallowing matter to pass through the baffle and out the suction portafter traversing at least a portion of the circumference of thecylindrical cavity wall. In some embodiments, the baffle comprises asolid portion disposed proximally to the input port, and means forpreventing liquids and/or solids in the flow from being pulled directlyfrom the input port to the suction port before traversing at least aportion of the circumference of the cylindrical cavity wall.

In some embodiments, the central member comprises a tapered sectiondisposed in the conical cavity, and means for directing the flow ofmatter within the separator. In some embodiments, the central membercomprises a plurality of cylindrical sections comprising differentdiameters, and means for directing the flow of matter within theseparator.

In some embodiments, a plurality of cylindrical sections include a firstsection that defines a first portion of the annular cavity and a secondsection that defines a second portion of the annular cavity, and meansfor directing the flow of matter within the separator. In someembodiments, the first portion is disposed between the baffle and thesecond portion, the second portion is disposed between the first portionand the conical cavity, and means for directing the flow of matterwithin the separator. In some embodiments, the central member furthercomprises a tapered section disposed in the conical cavity therebyforming a hollow cone shaped cavity, the hollow cone shaped cavitydisposed between the second portion and the second port, and means fordirecting the flow of matter through the hollow cone shaped cavity. Insome embodiments, the suction port of a first separator is coupled tothe input port of a second separator, and means for providing suction tothe first separator through the second separator.

In some embodiments, the system further comprises a means for allowingthe flow of matter to pass from the input port to the suction port ofthe first separator, when the canister corresponding to the firstseparator is filled to a capacity, to the second separator andcollecting at least a portion of the flow of matter in the canistercorresponding to the second separator. In some embodiments, the suctionsource comprises a vacuum pump, and means for providing vacuum to thesuction port.

In some embodiments, the suction source comprises a means for generatingsuction based on a Coanda effect. In some embodiments, the suctionsource comprises a means for generating suction based on a Venturieffect.

Another aspect of the present disclosure provides a separator for use ina medical environment. In some embodiments, the separator comprise: (a)a cylindrical cavity having a cylindrical cavity wall, a firstcylindrical cavity end, and a second cylindrical cavity end, theseparator configured to operate with the first cylindrical cavity endbeing up; (b) an suction port to be coupled to an operating room suctionsource, the suction port being in the first cylindrical cavity end; (c)a conical cavity, the conical cavity having a wide end and a narrow end,the wide end being mated to the second cylindrical cavity end; (d) ancollection port at the narrow end of the conical cavity; (e) an inputport to receive a flow comprising a mixture of liquid and gas, the inputport being in the cylindrical cavity wall, the flow to be induced intothe separator by the suction source, the input port configured to directliquids in the flow to cling to the cylindrical cavity wall; (f) abaffle disposed between the input port and the suction port, the baffleto prevent liquids in the flow from being pulled directly from the inputport to the suction port without traversing at least a first portion ofa circumference of the cylindrical cavity wall, the baffle to allowgasses in the flow to separate from the liquids in the flow and bepulled out of the separator via the suction port; and (g) a cylindricalcentral member disposed within the cylindrical cavity, the centralmember disposed to form an annular cavity between the central member andthe cylindrical cavity wall, the liquids in the flow to pass through theannular cavity before dropping out the collection port.

In some embodiments, the flow further comprises solids, the solids inthe flow to pass through the annular cavity before dropping out thesecond port. In some embodiments, the liquids include intracellularfluids and extracellular fluids. In some embodiments, the liquidsinclude blood. In some embodiments, the gas comprises smoke generatedfrom electrosurgical tools comprising a bovie, harmonic scalpel,electrosurgical pencil and laser.

In some embodiments, the baffle comprises a plurality of openings toallow the gasses in the flow be pulled out of the separator via thefirst port. In some embodiments, the baffle comprises a solid portionthat prevents liquids in the flow from being pulled directly from thecollection port to the first port, the solid portion corresponding to atleast the first portion of the circumference.

In some embodiments, the central member comprises a tapered sectiondisposed in the conical cavity. In some embodiments, the central membercomprises a plurality of cylindrical sections comprising differentdiameters.

In some embodiments, a plurality of cylindrical sections includes afirst section that defines a first portion of the annular cavity and asecond section that defines a second portion of the annular cavity. Insome embodiments, the first portion is disposed between the baffle andthe second portion, the second portion is disposed between the firstportion and the conical cavity. In some embodiments, the central memberfurther comprises a tapered section disposed in the conical cavitythereby forming a hollow cone shaped cavity, the hollow cone shapedcavity disposed between the second portion and the second port.

Another aspect of the present disclosure provides a method of operatinga separator in a medical environment. In some embodiments, the methodcomprises: (a) providing one or more fluid separators, wherein a fluidseparator comprises: (i) a cylindrical cavity comprising a cylindricalcavity wall, a first cylindrical cavity end, and a second cylindricalcavity end, the fluid separator configured to operate with the firstcylindrical cavity end being up; (ii) an suction port operativelycoupled to a suction source, the suction port being in the firstcylindrical cavity end; (iii) a conical cavity, the conical cavitycomprising a wide end and a narrow end, the wide end mated to the secondcylindrical cavity end; (iv) an collection port at the narrow end of theconical cavity; (v) an input port to receive a flow comprising a mixtureof liquid and gas, the input port being in the cylindrical cavity wall,the flow to be induced into the separator by the suction source, theinput port configured to direct liquids in the flow to cling to thecylindrical cavity wall; (vi) a baffle disposed between the input portand the suction port, the baffle to prevent liquids in the flow frombeing pulled directly from the input port to the suction port withouttraversing at least a first portion of a circumference of thecylindrical cavity wall, the baffle to allow gasses in the flow toseparate from the liquids in the flow and be pulled out of the separatorvia the suction port; and (vii) a cylindrical central member disposedwithin the cylindrical cavity, the central member disposed to form anannular cavity between the central member and the cylindrical cavitywall, the liquids in the flow to pass through the annular cavity beforedropping out the collection port; (b) attaching the one or moreseparators each to an associated waste deposit; (c) attaching thesuction port to a suction source; (d) activating the suction source,thereby creating flow through the one or more separators; (e) directingthe flow using the cylindrical cavity and cylindrical central member toseparate element comprising the flow; (f) ejecting liquids and/or solidsfrom the collection port that have been separated from the flow; and (g)pulling the gas out of the suction port using the suction source. Insome embodiments, the method further comprises providing a canister asthe waste deposit.

In some embodiments, attaching the suction port to a suction sourcecomprises attaching the suction port of a first separator to the inputport of a second separator that is attached to a suction source. In someembodiments, the method further comprises attaching the input port of aseparator to a suction device. In some embodiments, the method furthercomprises attaching the suction device to a surgical instrument.

In some embodiments, the method further comprises operating the one ormore separators in series by coupling the suction port of one separatorto the input port of another separator, coupling the suction port of thelast separator in the series of separators to the suction source andreceiving the flow at the input of the first separator in the series ofseparators. In some embodiments, the method further comprises receivingmatter into the input port of a first separator in a series ofseparators via the suction source applied to the suction port of a lastseparator in the series of separators, pulling gas out of the suctionport of another separator in the series of separators while anassociated canister is filled below a predetermined capacity expellingportions of the flow out of the collection port of another separator inthe series of separators until an associated canister is filled to apre-determined limit. In some embodiments, the method further comprisespassing the flow, unseparated, from the input port out of the suctionport of the first separator in the series of separators when the flow isno longer ejecting from the collection port of the first separator tothe input port of another separator ejecting the flow, or portionsthereof, out of the collection port.

Another aspect of the present disclosure provides a system forseparating a flow of matter. In some embodiments, the system comprises:(a) a flow separation device comprising: (i) a hollow body comprising afirst end, a second end, and an inner volume therebetween; (ii) asuction port disposed at the first end; (iii) a collection port disposedat the second end; (iv) an input port disposed between the first end andthe second end and in fluid communication with the inner volume; (v) oneor more baffles disposed within the inner volume between the first endand the second end; and (vi) a shaft disposed within the inner volume,(b) a surgical instrument; and (c) a suction source; wherein the inputport is configured to receive the flow of matter from the surgicalinstrument, the flow of matter comprising a gas, a liquid, a solid, orany combination thereof, wherein the shaft is configured to direct theflow of matter received into the hollow body, and wherein at least aportion of a liquid of the flow of matter exits the hollow body from aport different than a port from which at least a portion of a gas of theflow of matter exits.

In some embodiments, the shaft directs at least a portion of the flow ofmatter in a cyclonic pattern along an inner surface of the hollow body.In some embodiments, the gas exits the suction port and the liquid exitsthe collection port.

In some embodiments, the one or more baffles are configured to preventthe flow of matter from passing directly from the input port to thesuction port without first traversing at least a portion of acircumference of an inner surface of the hollow body. In someembodiments, the one or more baffles comprise a plurality of openingsconfigured to receive at least a portion of the flow of matter. In someembodiments, the plurality of openings is distal to the input port. Insome embodiments, the one or more baffles comprise a tapered section orcomprise a plurality of cylindrical sections comprising differentdiameters.

In some embodiments, the second end comprises a conical shape. In someembodiments, the hollow body comprises a cylindrical shape. In someembodiments, the flow of matter comprises surgical waste. In someembodiments, the flow of matter comprises biological material.

In some embodiments, the input port is proximal to the suction port anddistal from the collection port. In some embodiments, the suction portis configured to couple to the suction source. In some embodiments, thesuction source is a passive suction source.

In some embodiments, the collection port is configured to couple to acollection container. In some embodiments, the flow separation device isattachable or formed therein a collection container. In someembodiments, the one or more baffles aids in the separation of gas, ofliquid, or a combination thereof from the flow of matter.

In some embodiments, the input port forms an angle relative to a centralaxis of the hollow body that is less than 90 degrees forming an angledinput port. In some embodiments, the angled input port enhances entry ofthe flow of matter into the angled input port, enhances a cyclonicpattern of flow along an inner surface of the hollow body, or acombination thereof.

In some embodiments, the flow separation device enhances a suctioncapacity of the surgical instrument operatively coupled to the inputport. In some embodiments, the suction capacity is increased at leastabout 1.25 fold compared to a surgical instrument not operativelycoupled to a flow separation device. In some embodiments, the flowseparation device is disposable.

In some embodiments, the system further comprises one or more filters.In some embodiments, the one or more filters are disposed adjacent tothe collection port. In some embodiments, a pore size of the one or morefilters is less than about 1 micron. In some embodiments, the one ormore filters collect one or more solids. In some embodiments, the one ormore solids are a bacterium, a bacterial fragment, a bacterial particle,a virus, a viral fragment, a viral particle, or any combination thereof.

In some embodiments, the system further comprises one or more positivelycharged matrices, one or more negatively charged matrices, or anycombination thereof. In some embodiments, the one or more positivelycharged matrices, the one or more negatively charged matrices, or anycombination thereof are operatively connected to the suction port. Insome embodiments, the flow separation device is operatively coupled toone or more surgical instruments, one or more suctioning devices, one ormore suction sources, one or more canisters, one or more filtrationunits, one or more charged matrices, or any combination thereof.

Additional aspects and advantages of the present disclosure will becomereadily apparent to those skilled in this art from the followingdetailed description, wherein only illustrative embodiments of thepresent disclosure are shown and described. As will be realized, thepresent disclosure is capable of other and different embodiments, andits several details are capable of modifications in various obviousrespects, all without departing from the disclosure. Accordingly, thedrawings and description are to be regarded as illustrative in nature,and not as restrictive.

INCORPORATION BY REFERENCE

All publications, patents, and patent applications mentioned in thisspecification are herein incorporated by reference to the same extent asif each individual publication, patent, or patent application wasspecifically and individually indicated to be incorporated by reference.

BRIEF DESCRIPTION OF THE DRAWINGS

The novel features of the subject matter described herein are set forthwith particularity in the appended claims. A better understanding of thefeatures and advantages of the present subject matter will be obtainedby reference to the following detailed description that sets forthillustrative embodiments, in which the principles of the subject matterdescribed herein are utilized, and the accompanying drawings of which:

FIG. 1 is a block diagram illustrating a separator.

FIG. 2A is a block diagram illustrating a separator and canister system.

FIG. 2B is a diagram illustrating the operation of a separator andcanister system.

FIG. 3 is a diagram illustrating a method of operating a separator andcanister system.

FIG. 4A is a block diagram illustrating a separator system.

FIG. 4B is a block diagram illustrating the operation of a separatorsystem.

FIG. 4C is a block diagram illustrating the operation of a separatorsystem.

FIG. 5 is a diagram illustrating a method of operating a separatorsystem.

FIG. 6 is a block diagram illustrating a suction system.

FIG. 7 is a diagram illustrating a method of operating a suction system.

FIG. 8A is an exploded-view diagram illustrating a separator.

FIG. 8B is a diagram illustrating a shaft (such as a vortex element).

FIG. 8C is a top-view diagram illustrating the operation of a separator.

FIG. 8D is a cross-section diagram illustrating the operation of aseparator.

FIG. 9A is an exploded-view diagram illustrating a separator.

FIG. 9B is a diagram illustrating a shaft (such as a vortex element).

FIG. 9C is a top-view diagram illustrating the operation of a separator.

FIG. 9D is a cross-section diagram illustrating the operation of aseparator.

FIG. 10A is an exploded-view diagram illustrating a separator.

FIG. 10B is a diagram illustrating a shaft (such as a vortex element).

FIG. 10C is a top-view diagram illustrating the operation of aseparator.

FIG. 10D is a cross-section diagram illustrating the operation of aseparator.

FIG. 11A is an exploded-view diagram illustrating a separator.

FIG. 11B is a top-view diagram illustrating the operation of aseparator.

FIG. 11C is a cross-section diagram illustrating the operation of aseparator.

FIG. 12 is a diagram illustrating a separator system.

FIG. 13A is a block diagram illustrating a separator with filter.

FIG. 13B is a block diagram illustrating a separator with filter.

FIG. 13C is a block diagram illustrating a separator with filter.

FIG. 14 is a block diagram illustrating a separator canister system.

FIG. 15 is a block diagram illustrating a separator.

FIG. 16 is a block diagram illustrating a separator.

FIG. 17 is a block diagram illustrating a separator system.

FIG. 18 is a block diagram illustrating a separator with check valve.

FIG. 19 is a diagram illustrating the system in a surgical use setting.

FIG. 20A is a diagram illustrating a flow separation device attachableor formed therein a canister lid.

FIG. 20B is a diagram illustrating a flow separation device attachableor formed therein a canister lid.

FIG. 21A-B are diagrams illustrating a flow separation device with anangled input port.

FIG. 21C is a cross-section of a flow separation device with an angledinput port.

FIG. 21D is a top view of a flow separation device showing the relationbetween the input port and the baffle within the hollow body.

FIG. 22A is a cross-section of the flow separation device.

FIG. 22B is a top view of a flow separation device showing the relationbetween the input port and the baffle within the hollow body.

FIG. 23A-B are diagrams illustrating a helical baffle.

FIG. 23C is a diagram illustrating a flow path into the input port ofthe flow separation device.

FIG. 23D is a cross-section of the flow separation device illustratingthe helical baffle.

FIG. 24A is a diagram illustrating the shaft with a bulbous end.

FIG. 24B-C are diagrams illustrating the openings on a baffle of thedevice.

DETAILED DESCRIPTION

While various embodiments have been shown and described herein, it willbe obvious to those skilled in the art that such embodiments areprovided by way of example only. Numerous variations, changes, andsubstitutions may occur to those skilled in the art without departingfrom the subject matter described herein. It should be understood thatvarious alternatives to the embodiments of the subject matter describedherein is employed.

FIG. 1 is a block diagram illustrating separator 100. In operation,separator 100 is configured to separate liquids, solids and gasses in aflow of matter. Separator 100 ejects liquids and/or solids separatedfrom the flow of matter out collection port 108 while suctioning atleast gasses separated from the flow of matter out suction port 106.Separator 100 is operated by suction received from a suction source. Itshould be understood that the terms “suction” and “vacuum” as usedherein refer to a pressure below the surrounding ambient air pressure.

In some embodiments, separator 100 comprises hollow body 102, input port104, suction port 106, collection port 108, baffle 110, and shaft 112.

In some embodiments, hollow body 102 comprises a cylindrical walldefining a cylindrical cavity. Other hollow body 102 shapes are suitablefor use with the separator 100 including conical shapes and ovoidcylindrical shapes. The hollow body 102 wall may include a first cavityend and a second cavity end. The cavity of hollow body 102 may have awide end and a narrow end. Hollow body 102 is constructed of a singlesolid wall that is formed into the hollow body 102 shape, oralternatively, a first wide end of hollow body 102 is mated to a secondnarrow end of hollow body 102 to form a single hollow body 102 having anarrow section and wide section. In some embodiments, hollow body 102 isconfigured to operate in an orientation with the first cavity end up.Hollow body 102 is configured to be oriented in operation to allowgravity to pull at least liquid and solids separated from a flow ofmatter out collection port 108, while gasses separated from the flow ofmatter are pulled by suction out of suction port 106.

Input port 104 is configured to receive a flow of matter. In someembodiments, input port 104 is integral to hollow body 102. Input port104 is disposed in the cylindrical cavity wall. Input port 104 islocated off-axis from an axis defined by the longitudinal center of thecylindrical cavity.

Input port 104 is configured and positioned to direct a flow of matterreceived into the hollow body 102 along the internal cavity wall of thehollow body 102. Because, in some embodiments, the hollow body 102comprises a cylindrical, spherical, or ovoid cylindrical shape, the flowgenerated within the cavity of the hollow body 102 comprises andessentially cyclonic flow pattern.

By directing the flow of matter along the internal cavity wall of thehollow body 102, forming a cyclonic flow pattern, liquids, solids, andgasses will tend to cling to the wall of the internal cavity wall ofhollow body 102 due to the effects of centripetal forces.

A flow of matter is induced into separator 100 by suction received fromsuction port 106 by a suction or vacuum source. In some embodiments,suction port 106 further comprises a check valve mechanism (not shown inFIG. 1 ) to, for example, prevent the flow of solids or liquids throughsuction port 106.

Suction port 106 is configured to couple to a suction source. In certainembodiments, the suction source may include, for example, a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 106 to input port104. Suction port 106 is disposed near the first cavity end of thehollow body 102. Suction port 106 provides suction received from asuction source for operating separator 100 and may further comprise acheck valve. In some embodiments, suction port 106 includes fittingsconfigured to attach tubing. For example, barbed or quick-disconnecttype fittings are used to couple tubing to suction port 106. The tubingis, for example, used to couple suction port 106 to a suction source orto an input port 104 of another separator.

Collection port 108 is configured to expel at least liquids and/orsolids. Collection port 108 is disposed at the narrow end of the conicalcavity of hollow body 102. In some embodiments, collection port 108 isconfigured to couple to a canister. A canister is used to collect andmeasure matter received from separator 100. A canister may also be usedfor the safe collection, transportation and disposal of waste receivedfrom separator 100. In some embodiments, collection port 108 is coupledto tubing or piping to direct matter to a waste drain. In someembodiments, collection port 108 may include a mounting ring configuredto form a seal between collection port 108 to tubing or a canister.

Baffle 110 is disposed between input port 104 and suction port 106.Baffle 110 is configured to facilitate a cyclonic flow of matter withinthe hollow cavity 100 by preventing liquids and/or solids in the flowfrom being pulled directly from input port 104 to suction port 106without traversing at least a first portion of a circumference of thecylindrical wall of hollow body 102. In some embodiments, baffle 110includes openings configured to allow at least gasses in a flow ofmatter to separate from liquids and/or solids that are included in theflow. One or more gasses are pulled through baffle 110 and out suctionport 106. In some embodiments, baffle 110 includes a solid surfacelocated proximal to input port 104. The solid surface included in baffle110 is used to prevent liquids and/or solids in the flow from beingpulled directly from input port 104 to suction port 106 by allowing timefor gravity to act on the liquids and/or solids before they reach anopening in baffle 110. In some embodiments, a baffle 110 comprises botha solid surface portion and a portion with an opening. In theseembodiments, the solid surface portion of the baffle 110 is positionedrelative to the input port 104 in such a way that gravity acts on aliquid and/or solid within the cyclonic flow before a suction forcethrough suction port 106 draws the liquid and/or solid out of theopening portion of the baffle 110. The solid surface portion of thebaffle 110 is thus configured to prevent suction of liquid and/or solidmatter out of suction port 106 while allowing time for gravity to act onthe liquids and/or solids as they traverse the solid surface of baffle110. The effect of gravity within the cavity of the hollow body 102 onliquids and/or solids causes them to generally descend (within the inputflow) towards collection port 108 and thereby not be suctioned out ofthe suction port 106.

Shaft 112 is configured to direct a flow of matter in a cyclonic flow.The cyclonic flow along with gravity cause liquids and solids toseparate from gasses included in the flow of matter. In someembodiments, shaft 112 includes a member disposed within the cylindricalcavity of hollow body 102. The member of shaft 112 is positioned withinthe cavity of hollow body 102 so that the cavity of hollow body 102surrounding the central member of shaft 112 comprises an annular cavityshape between shaft 112 and hollow body 102 cavity wall.

Shaft 112 is configured to direct liquids and/or solids that are in theflow so that they pass through the annular cavity between the shaft 112and hollow body 102 cavity wall before dropping out collection port 108.In some embodiments, shaft 112 includes a tapered section or conical enddisposed in the cavity of hollow body 102. In some embodiments, shaft112 includes a plurality of sections having different diameters. Theplurality of sections, for example, include a first cylindrical sectionthat defines a first portion of the annular section of the cavity thehollow body 102 and a second section that defines a second portion ofthe annular cavity. Tapered and cylindrical sections of shaft 112 areconfigured to direct the flow within hollow body 102 in a cyclonic flowpattern. In some embodiment, baffle 110 is integral to shaft 112.

FIG. 2A is a block diagram illustrating separator and canister system200. Separator 202 is an example of separator 100; however, separator202 may include alternative configurations and methods of operation.Separator and canister system 200 may include separator 202 and canister214.

In some embodiments, separator 202 comprises input port 204, suctionport 206, collection port 208, baffle 210 and shaft 212.

In some embodiments, separator 202 comprises a generally cylindricalcavity and a cavity wall. Non-limiting examples of other suitable cavityshapes for separator 202 include spherical and ovoid cylindrical shapes.

Separator 202 is configured to generate a vortex flow within the cavityof separator 202. The cavity of separator 202 includes a first end and asecond cavity end. In some embodiments, the cavity is configured to havea wide end and a narrow end. The wide end is coupled to the second endof the generally cavity. In some embodiments, the separator 202 isconfigured to operate with the first end positioned upwards.

Input port 204 is configured to direct a flow of matter into separator202. Input port 204 also directs the flow of matter towards shaft 212.The flow of matter may include liquids, solids and gasses, includingcombinations thereof in varying ratios. Some constituents of the flow ofmatter may include surgical byproducts. A flow of matter is induced intoinput port 204 by suction received from a suction source. In someembodiments, input port 204 is integral to separator 202. Input port 204is disposed in the cavity wall near the first end of the generallycylindrical cavity of separator 202. Input port 204 is disposed off-axisfrom an axis defined by the longitudinal center of the generallycylindrical cavity of the body. In an embodiment, input port 204 mayinclude fittings such as, barbed or quick-disconnect type fittings, forcoupling input port 204 to a suction tip or surgical device. In someembodiments, input port 204 is configured and positioned to generate avortex of flow within the cavity of the separator 202.

Suction port 206 is configured to couple to a suction source. In certainembodiments, the suction source may include a vacuum pump, aspirator,and/or a positive pressure operated suction source—such as suctionsources that take advantage of Venturi or Coanda effect. Suction from asuction source is transferred from suction port 206 to input port 204.Suction port 206 is disposed near the first cylindrical cavity end.Suction port 206 provides suction received from a suction source foroperating separator and canister system 200. In some embodiments,suction port 206 may include fittings configured to attach tubing. Forexample, barbed or quick-disconnect type fittings are used to coupletubing to suction port 206. The tubing is used to couple suction port206 to a suction source or to an input port 204 of another separator.

Collection port 208 is configured to expel at least liquids and/orsolids separated from a flow of matter received at input port 204.Collection port 208 is disposed at the narrow end of the conical cavityof the hollow body of separator 202. Collection port 208 is configuredto couple separator 202 to canister 214. In some embodiments, collectionport 208 includes a mounting ring configured to form a seal whenseparator 202 is coupled to canister 214, tubing, piping or some otherelement configured to dispose of at least liquids and/or solids. In someembodiments, collection port 208 may include fittings, such as barbed orquick disconnect type fittings for, for coupling collection port 208 tocanister 214 or tubing.

Baffle 210 is configured to allow gasses to be pulled out suction port206 from liquids and/or solids in a flow of matter received at inputport 204. Baffle 210 is configured to prevent liquids or solids in aflow of matter received at input port 204 from being pulled directlyfrom input port 204 to suction port 206 without traversing at least afirst portion of a circumference of separator 202. Baffle 210 isdisposed between input port 204 and suction port 206. In an embodiment,baffle 210 includes a plurality of openings to allow at least the gassesin a flow of matter to be pulled out suction port 206. In an embodiment,baffle 210 includes a solid surface located proximal to input port 204.The solid surface is configured to prevent liquids and/or solids in aflow of matter from being pulled directly from input port 204 to suctionport 206 without first traversing at least a portion of separator 202 asdescribed with reference to FIG. 1 .

Shaft 212 is configured to form an annular cavity between shaft 212 andseparator 202 within the cavity of separator 202. In some embodiments,shaft 212 includes a cylindrical central member disposed within thegenerally cylindrical cavity of separator 202. Shaft 212 is configuredto generate a vortex flow within separator 202. The vortex flow andgravity cause liquids and/or solids in a flow of matter received atinput port 204 to separate from gasses. Liquids and gases within thematter flow are expelled out suction port 206. In an embodiment, shaft212 may include a tapered section disposed near the conical cavity ofseparator 202. In some embodiments, shaft 212 may include a plurality ofcylindrical sections having different diameters. In some embodiments,the plurality of cylindrical sections may include a first section thatdefines a first portion of the annular cavity and a second section thatdefines a second portion of the annular cavity. In some embodiments,baffle 210 is integral to shaft 212.

Canister 214 is configured to receive waste from separator 202. Thewaste may include at least liquids and/or solids separated from a flowof matter received at input port 204. Canister 214 is used to measurethe amount of liquids and/or solids separated from the flow of matterreceived at input port 204. Canister 214 is configured to permit thesafe collection, transportation and disposal of waste. In someembodiments, canister 214 may include a valve configured to activatewhen canister 214 is filled to a pre-determined volume. The valve isused to prevent waste from leaving canister 214 during transportation.In some embodiments, canister 214 may include a commercially availablecanister.

FIG. 2B is a diagram illustrating the operation of separator andcanister system 200. In addition to the elements illustrated in FIG. 2A,FIG. 2B includes input flow 240, suction flow 242 and collection flow244.

In operation, a suction source is coupled to suction port 206 togenerate suction flow 242. The suction source may include a vacuum pump,aspirator or a Coanda based suction generator. Suction flow 242generates a flow within separator 202. Suction flow 242 induces inputflow 240 to enter input port 204. Input flow 240 may include liquids,solids, and gasses, including combinations thereof in varying ratios.Some constituents of input flow 240 may include surgical byproducts.Suction flow 242 may generate a cyclonic or vortex flow within separator202 in order to separate liquids, solids and gasses from input flow 240.

Shaft 212 in conjunction with separator 202 is configured to generate acyclonic or vortex flow from input flow 240 using suction flow 242.Baffle 210 may prevent input flow 240 from passing directly from inputport 204 to suction port 206 without first traversing at least a portionof separator 202. The cyclonic flow, along with gravity, separatescollection flow 244 and suction flow 242 from input flow 240. One ormore gasses are separated from input flow 240 is pulled out suction port206 as suction flow 242.

Suction flow 242 is directed out of separator 202 by suction port 206.Suction port 206 is configured to exhaust at least suction flow 242 fromseparator 202. In some methods of operation, suction port 206 expelsinput flow 240, unseparated, out of suction port 206.

Collection flow 244 is directed out of collection port 208. Collectionport 208 is configured to expel at least collection flow 244 fromseparator 202. Collection port 208 is configured to direct collectionflow 244 to canister 214.

In some embodiments, canister 214 is connected to a suction source (notshown). The suction transferred to canister 214 from the suction sourceprovides an additional pull on the fluid and solid matter in separator202 (i.e. in addition to gravity) to facilitate separation of liquid andsolid matter (drawn into canister 214) from gas (drawn out throughsuction port 206).

FIG. 3 is a diagram illustrating a method of operating a separator andcanister system. The steps illustrated in FIG. 3 is performed by, forexample, one or more elements of separator and canister system 200.

In a step 302, a suction source is applied to a suction port. In someembodiments, said suction port is part of a separator system asdescribed herein. In some embodiments, a user connects a suction port toa suction source that comprises an air amplifier based on a Coanda orVenturi effect. In some embodiments, the suction is applied to a suctionport of a device configured to separate suctioned matter that wassuctioned from a surgical field during a surgical procedure. As appliedbut not limited to canister system 200, a separator 202 includes suctionport 206. Suction port 206 is configured to couple to a suction sourcecapable of providing suction flow 242. A suction source is configured toapply suction flow 242.

In a step 304 a cyclonic or vortex flow is generated by a separatorsuch, as for example, separator 100 or separator 200. A cyclonic orvortex flow is generated from a suction flow applied to a suction portof a separator. In some embodiments, a cyclonic or vortex suction flowis generated when air within the separator is suctioned through thesuction port as a result of an application of a suction flow. A shaftwithin the separator cavity is configured to create a cyclonic flowwithin the separator, and air within the separator cavity that issuctioned out with the initial application of suction to the separatoris drawn around the shaft to form a cyclonic or vortex flow. In someembodiments, the shaft further comprises a conical head that furtherpromotes cyclonic flow. In some embodiments, the cyclonic or vortex flowof suction causes matter comprising a solid, a liquid, a gas, or acombination thereof to be drawn into the separator in a cyclonic orvortex input flow. In some embodiments, the position of the input portfurther aids in generating a cyclonic or vortex flow of an input flow.In some embodiments, the inlet port is positioned towards the upperportion of the separator. In some embodiments, the inlet port ispositioned at an angle such that it directs an inflow essentiallydirectly against an interior wall surface of the separator cavity. Asapplied but not limited to system 200, separator 202 is configured togenerate, from suction flow 242, a cyclonic flow of matter that isreceived via input port 204.

In a step 306, an input flow is received via an input port. Suction flowgenerates suction at an input port. Suction flow is at a pressure belowan ambient air pressure. Therefore, a suction flow causes input flowwhich is at around ambient pressure to be received at an input port ofthe separator device. In some embodiments, the input flow comprises asolid, liquid, a gas, or a combination thereof. In some embodiments, theinput flow travels in a cyclone or vortex flow pattern within theseparator. As applied but not limited to system 200, input port 204 isconfigured to receive input flow 240. Suction flow 242 generates suctionat input port 204. Suction flow 242 is at a pressure below an ambientair pressure. Therefore, suction flow 242 causes input flow 240 to bereceived at input port 204.

In a step 308, the components of an input flow comprising a mixture of asolid and/or a liquid with a gas are separated. For example, a separatoris configured to separate a solid and/or liquid from a gas of an inputflow by directing the heavier constituents (i.e., liquids and/or solids)of the input flow into a cyclonic flow pattern that gravity acts upon tocause these heavier constituents to exit via collection port, while thelighter constituents (i.e. gasses, smoke, aerosols) in the input flow ispulled out of separator by the suction at the suction port. Thus, acollection flow that is released from the separator via a collectionport includes at least liquids and/or solids. As applied but not limitedto system 200, separator 202 is configured to separate collection flow244 from input flow 240 by directing the heavier constituents (i.e.,liquids and solids) of input flow 240 into a cyclonic flow pattern thatgravity acts upon to cause these heavier constituents to exit viacollection port 208, while the lighter constituents (i.e. gasses, smoke,aerosols) in input flow 240 are pulled out of separator 202 by thesuction at suction port 206. Thus, collection flow 244 includes at leastliquids and/or solids.

In a step 310, the separated solid and/or liquid from the input flow aredirected into a collection port. For example, a collection port isconfigured to receive the heavier constituents and direct them to acanister. Liquids and/or solids are collected in a canister. Forexample, a canister is configured to receive a collection flow (whichmay include liquids and/or solids) from collection port. As applied butnot limited to system 200, collection port 208 is configured to receivethe heavier constituents and direct them to collection canister 214.

In a step 312, the separated solid and/or liquid is collected in acollection canister. As applied but not limited to system 200,collection canister 214 is configured to receive collection flow 244(which may include liquids and solids) from collection port 208.

In a step 314, gasses are suctioned through a suction port. For example,a suction flow may include gasses drawn out of an input flow. Suctionport is configured to allow suction flow to be suctioned through suctionport. In some embodiments, a separator further comprises a baffle thatprevents liquids and/or solids within an input flow to be suctioned fromthe suction port by the suction flow. As applied but not limited tosystem 200, suction flow 242 may include gasses. Suction port 206 isconfigured to allow suction flow 242 to be suctioned through suctionport 206.

FIG. 4A is a block diagram illustrating separator system 400. In thisembodiment, one or more separator systems are aligned in series. Asshown, separator 402 and separator 422 are examples of separator 202;however separator 402 and separator 422 may include alternativeconfigurations and methods of operation.

In some embodiments, separator system 400 may, for example, includeseparator 402, canister 414, separator 422, canister 434 and suctionsource 416.

Separator 402 is configured to generate a vortex flow within the cavityof separator 402. The cavity of separator 402 includes a first end and asecond cavity end. In some embodiments, the cavity is configured to havea wide end and a narrow end. The wide end is coupled to the second endof the generally cavity. In some embodiments, the separator 402 isconfigured to operate with the first end positioned upwards.

Input port 404 is configured to direct a flow of matter into separator402. Input port 404 directs the flow of matter towards shaft 412. Theflow of matter may include liquids, solids and gasses, includingcombinations thereof in varying ratios. Some constituents of the flow ofmatter may include surgical byproducts. A flow of matter is induced intoinput port 404 by suction received from a suction source. In someembodiments, input port 404 is integral to separator 402. Input port 404is disposed in the cavity wall near the first end of the generallycylindrical cavity of separator 402. Input port 404 is disposed off-axisfrom an axis defined by the longitudinal center of the generallycylindrical cavity of the body. In an embodiment, input port 404 mayinclude fittings such as, barbed or quick-disconnect type fittings, forcoupling input port 404 to a suction tip or surgical device. In someembodiments, input port 404 is configured and positioned to generate avortex of flow within the cavity of the separator 402.

Suction port 406 is configured to couple to a suction source. In certainembodiments, the suction source may include a vacuum pump, aspirator,and/or a positive pressure operated suction source—such as suctionsources that take advantage of Venturi or Coanda effect. Suction from asuction source is transferred from suction port 406 to input port 204.Suction port 406 is disposed near the first cylindrical cavity end.Suction port 406 may provide suction received from a suction source foroperating separator and canister system 400. In some embodiments,suction port 406 may include fittings configured to attach tubing. Forexample, barbed or quick-disconnect type fittings are used to coupletubing to suction port 406. The tubing is used to couple suction port406 to a suction source or to an input port 404 of another separator.

Collection port 408 is configured to expel at least liquids and/orsolids separated from a flow of matter received at input port 404.Collection port 408 is disposed at the narrow end of the conical cavityof the hollow body of separator 402. Collection port 408 is configuredto couple separator 402 to canister 414. In some embodiments, collectionport 408 includes a mounting ring configured to form a seal whenseparator 402 is coupled to canister 414, tubing, piping or some otherelement configured to dispose of at least liquids and/or solids. In someembodiments, collection port 408 may include fittings, such as barbed orquick disconnect type fittings for, for coupling collection port 408 tocanister 414 or tubing.

Baffle 410 is configured to allow gasses to be pulled out suction port406 from liquids and/or solids in a flow of matter received at inputport 404. Baffle 410 is configured to prevent liquids or solids in aflow of matter received at input port 404 from being pulled directlyfrom input port 404 to suction port 406 without traversing at least afirst portion of a circumference of separator 402. Baffle 410 isdisposed between input port 404 and suction port 406. In someembodiments, baffle 410 includes a plurality of openings to allow atleast the gasses in a flow of matter to be pulled out suction port 406.In some embodiments, baffle 410 includes a solid surface locatedproximal to input port 404. The solid surface is configured to preventliquids and/or solids in a flow of matter from being pulled directlyfrom input port 404 to suction port 406 without first traversing atleast a portion of separator 402 as described with reference to FIG. 1 .

Shaft 412 is configured to form an annular cavity between shaft 412 andseparator 402 within the cavity of separator 402. In some embodiments,shaft 412 includes a cylindrical central member disposed within thegenerally cylindrical cavity of separator 402. Shaft 412 is configuredto generate a vortex flow within separator 402. The vortex flow andgravity cause liquids and/or solids in a flow of matter received atinput port 404 to separate from gasses. Liquids and gases within thematter flow are expelled out suction port 406. In an embodiment, shaft412 includes a tapered section disposed near the conical cavity ofseparator 402. In some embodiments, shaft 412 includes a plurality ofcylindrical sections having different diameters. In some embodiments,the plurality of cylindrical sections includes a first section thatdefines a first portion of the annular cavity and a second section thatdefines a second portion of the annular cavity. In some embodiments,baffle 410 is integral to shaft 412.

Canister 414 is configured to receive waste from separator 402. Thewaste may include at least liquids and/or solids separated from a flowof matter received at input port 404. Canister 414 is used to measurethe amount of liquids and/or solids separated from the flow of matterreceived at input port 404. Canister 414 is configured to permit thesafe collection, transportation and disposal of waste. In someembodiments, canister 414 may include a valve configured to activatewhen canister 414 is filled to a pre-determined volume. The valve isused to prevent waste from leaving canister 414 during transportation.In some embodiments, canister 414 may include a commercially availablecanister.

Separator 422 may include similar configurations and methods ofoperation as separator 402. For the sake of brevity, separator 422 willnot be described further. Likewise collection canister 434 may includesimilar configurations and methods of operation as collection canister414. For the sake of brevity, collection canister 434 will not bedescribed further.

Separator system 400 includes suction source 416. Suction source 416 maybe any device configured to generate a pressure below an ambient airpressure. Suction source 416 may include a vacuum pump, aspirator orCoanda based positive pressure operated suction source.

FIG. 4B is a block diagram illustrating an exemplary operation ofseparator system 400 in a first mode. Separators 402, 422 are configuredto direct input flow 440 directly from input port 404 out suction port406 when canister 414 reaches a predetermined fill volume. Asillustrated in FIG. 4B, canister 414 may not have reached apredetermined fill volume. Fill volume 436 is less than thepredetermined fill volume.

In operation, suction source 416 supplies suction flow 442 to suctionport 426. Separator 422 is configured to transfer suction flow 442 toseparator 402. Suction flow 442 creates a pressure near input port 404that is below an ambient air pressure. The ambient air pressureovercomes the pressure of suction flow 442 thereby inducing input flow440 into input port 404. Input port 404 is configured to receive inputflow 440. Input flow 440 comprises liquids, gasses and solids, includingcombinations thereof in varying ratios. Input flow 440 may includesurgical byproducts. Shaft 412, in combination with an interior cavityof separator 402, creates a cyclonic flow within separator 402 fromsuction flow 442. The cyclonic flow and gravity causes collection flow444 to separate from input flow 440. Collection flow 444 comprises atleast liquids and/or solids. Collection flow 444 is expelled fromcollection port 408. Collection port 408 is configured to directcollection flow 444 to canister 444.

Fill volume 436 represents a volume of collection flow 444 contained incanister 414. As illustrated in FIG. 4B, fill volume 436 may not havereached a predetermined fill volume. In this case, separator 402operates in a first mode of operation. Separator 402 separates suctionflow 442 from collection flow 444. In the first mode of operation,suction flow 442 comprises primarily gasses separated from input flow440.

Suction flow 442 is pulled from separator 402 by suction source 416.Suction flow 442 is passed from suction port 406 to input port 424.Suction flow 442 may comprise primarily liquids and gasses. Separator402 continues to operate in the first mode of operation until fillvolume 436 reaches a predetermined volume.

In some embodiments, separator system 400 comprises a connection betweencanisters 414 and 434 (not shown). The connection between canisters isconfigured to transfer a suction force between canister 434 to canister414 and may comprise any of the means of transmitting suction describedherein including, for example, suction tubing. In this embodiment,suction generated by suction source 416 is transmitted to canister 434of separator 442 and then through the connection between the canistersthe suction is transmitted to canister 414. The suction transferred tocanister 414 provides an additional pull on the fluid and solid matterin separator 402 (i.e. in addition to gravity) to facilitate separationof liquid and solid matter (drawn into canister 414) from gas (drawn outthrough suction port 406).

FIG. 4C is a block diagram illustrating an exemplary operation ofseparator system 400 in a second mode. Separators 402, 422 areconfigured to pass input flow 440 from input ports 404, 424 to suctionports 406, 426 unseparated when canisters 414, 434 reach predeterminedfill volumes. As illustrated in FIG. 4C, fill volume 436 has reached apredetermined fill volume for canister 414. In a second mode ofoperation, separator 402 passes input flow 440 through suction port 406to separator 422 unseparated.

In operation, suction source 416 is configured to supply a suction flow442 to suction port 426. Separator 422 is configured to pass suctionflow 442 to separator 402. Suction flow 442 pulls input flow 440 intoinput port 404. Separator 402 passes input flow 440 from input port 404to suction port 406 because fill volume 436 has reached a predeterminedfill volume for canister 414. Input flow 440 is received by input port424.

Fill volume 438, as shown, has not reached a predetermined fill volumefor canister 434. Separator 422 therefore separates collection flow 444from suction flow 442. Collection flow 444 may comprise liquids and/orsolids from input flow 440. Separator 422 separates suction flow 442from collection flow 444. Collection flow 444 is expelled out collectionport 428. Collection port 428 is coupled to canister 434. Canister 434is configured to receive collection flow 444 from collection port 428.Suction flow 442 is pulled out suction port 426 by suction source 416.

The systems, devices, and methods described herein are configured toseparate a gas from a liquid at a controlled rate. The controlled rateof suction applied by a system increases when one or more flowseparation devices are connected as described herein. As describedherein, two or more separators in a system are connected “in series” sothat suction from a suction source is transmitted from a first separatorto a second separator connected to the first separator as describedherein. In alternative embodiments, one or more separators are in asystem connected “in parallel” such that two or more interconnectedseparators (connected to each other as described) are both connected toone or more suction sources.

In some embodiments, a suction transmitted through one or moreseparators connected in a system is greater than a suction transmittedthrough a single separator. For example, if a surgical suctioninstrument is connected to the separator system, an increased suctionforce is transmitted at the surgical suction instrument when it isconnected to any the systems of FIG. 4A-4C than when the surgicalsuction instrument is connected to any of the systems of FIG. 2A-2C(i.e. greater suction experienced at the surgical suction instrumentwhen connected to two or more separators in a system as opposed to aconnection to only one separator).

When one or more flow separation devices are connected as describedherein, a flow rate may be generated of at least about 1 cubiccentimeter per second (cc/s), 2 cc/s, 3 cc/s, 4 cc/s, 5 cc/s, 6 cc/s, 7cc/s, 8 cc/s, 9 cc/s, 10 cc/s, 11 cc/s, 12 cc/s, 13 cc/s, 14 cc/s, 15cc/s, 16 cc/s, 17 cc/s, 18 cc/s, 19 cc/s, 20 cc/s, 25 cc/s, 30 cc/s, 35cc/s, 40 cc/s, 45 cc/s, 50 cc/s, 55 cc/s, 60 cc/s, 65 cc/s, 70 cc/s, 75cc/s, 80 cc/s, 85 cc/s, 90 cc/s, 95 cc/s, 100 cc/s or more. The systemmay separate gas from liquid at a rate of at least about 5 cc/s. Thesystem may separate gas from liquid at a rate of at least about 10 cc/s.The system may separate gas from liquid at a rate of at least about 20cc/s. The system may separate gas from liquid at a rate of at leastabout 30 cc/s. The system may separate gas from liquid at a rate of atleast about 40 cc/s. The system may separate gas from liquid as a rateof at least about 50 cc/s.

The one or more flow separation devices as described herein may providea separation of a flow, such as a separation of a gas and liquid in aflow at a flow rate of about 100 mmHg, 150 mmHg, 200 mmHg, 250 mmHg, 300mmHg, 350 mmHg, 400 mmHg, 450 mmHg, 500 mmHg, or more. A separate of aflow may occur at a flow rate of at least about 150 mmHg. A separationof a flow may occur at a flow rate of at least about 200 mmHg. Aseparation of a flow may occur at a flow rate of at least about 250mmHg. A separation of a flow may occur at a flow rate of at least about300 mmHg. A separation of a flow may occur at a flow rate of at leastabout 350 mmHg. A separation of a flow may occur at a flow rate of atleast about 400 mmHg. A separation of a flow may occur at a flow rate ofat least about 500 mmHg. A separation of a flow may occur at a flow ratefrom about 150 mmHg to about 350 mmHg. A separation of a flow may occurat a flow rate from about 200 mmHg to about 350 mmHg.

The one or more flow separation devices as described herein may beconfigured to cyclone a liquid portion of a flow into an outlet portadjacent or attached to canister and to divert a gas portion of a flowthrough a separate outlet port such as to a filtration device. The oneor more flow separation devices or one or more components of theseparation device may be disposable. The one or more flow separationdevices or one or more components of the separation device may bereusable.

The suction capacity of a surgical instrument operatively coupled to oneor more flow separation devices may increase compared to a surgicalinstrument not operatively coupled. The suction capacity may increaseabout 1 fold, 1.25 fold, 1.5 fold, 1.75 fold, 2 fold, 2.25 fold, 2.5fold, 2.75 fold, 3 fold, 3.25 fold, 3.5 fold, 3.75 fold, 4 fold, 4.25fold, 4.5 fold, 4.75 fold, 5 fold, or more. The suction capacity mayincrease by at least about 1.25 fold. The suction capacity may increaseby at least about 1.5 fold. The suction capacity may increase by atleast about 1.75 fold. The suction capacity may increase by at leastabout 2 fold. The suction capacity may increase by at least about 2.5fold. The suction capacity may increase by at least about 3 fold.

The suction capacity of a surgical instrument operatively coupled to oneor more flow separation devices may increase compared to a surgicalinstrument not operatively coupled. The suction capacity may increaseabout 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%,85%, 90%, 95% or more. The suction capacity may increase at least about25%. The suction capacity may increase at least about 30%. The suctioncapacity may increase at least about 35%. The suction capacity mayincrease at least about 40%. The suction capacity may increase at leastabout 45%. The suction capacity may increase at least about 50%. Thesuction capacity may increase at least about 55%. The suction capacitymay increase at least about 60%. The suction capacity may increase atleast about 65%. The suction capacity may increase at least about 70%.The suction capacity may increase at least about 75%. The suctioncapacity may increase at least about 80%. The suction capacity mayincrease at least about 85%. The suction capacity may increase at leastabout 90%.

The suction capacity of a suction source, such as a passive suctionsource, operatively coupled to one or more flow separation devices mayincrease compared to a suction source not operatively coupled. Thesuction capacity may increase about 1 fold, 1.25 fold, 1.5 fold, 1.75fold, 2 fold, 2.25 fold, 2.5 fold, 2.75 fold, 3 fold, 3.25 fold, 3.5fold, 3.75 fold, 4 fold, 4.25 fold, 4.5 fold, 4.75 fold, 5 fold, ormore. The suction capacity may increase by at least about 1.25 fold. Thesuction capacity may increase by at least about 1.5 fold. The suctioncapacity may increase by at least about 1.75 fold. The suction capacitymay increase by at least about 2 fold. The suction capacity may increaseby at least about 2.5 fold. The suction capacity may increase by atleast about 3 fold.

The suction capacity of a suction source, such as a passive suctionsource, operatively coupled to one or more flow separation devices mayincrease compared to a suction source not operatively coupled. Thesuction capacity may increase about 20%, 25%, 30%, 35%, 40%, 45%, 50%,55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95% or more.

The suction capacity may increase at least about 25%. The suctioncapacity may increase at least about 30%. The suction capacity mayincrease at least about 35%. The suction capacity may increase at leastabout 40%. The suction capacity may increase at least about 45%. Thesuction capacity may increase at least about 50%. The suction capacitymay increase at least about 55%. The suction capacity may increase atleast about 60%. The suction capacity may increase at least about 65%.The suction capacity may increase at least about 70%. The suctioncapacity may increase at least about 75%. The suction capacity mayincrease at least about 80%. The suction capacity may increase at leastabout 85%. The suction capacity may increase at least about 90%.

FIG. 5 is a diagram illustrating an exemplary method of operating aseparator system in series. The steps illustrated in FIG. 5 is performedby, for example, one or more elements of separator system 400.

In steps 502 and 504, a single suction source applies suction to asuction port of a second separator which is connected to a firstseparator. The first separator is connected to the second separator suchthat a suction flow generated within the second separator is translatedto the first separator. In some embodiments, the input port of thesecond separator is connected to the suction port of the first separatorby a suction conduit such as standard suction tubing. A suction sourceis directly applied to a suction port of a second separator generating asuction flow that is transmitted to the first separator. As applied butnot limited to system 400, suction source 416 is configured to supplysuction. Suction port 426 is configured to receive suction flow 442 fromsuction source 416. Separator 422 is configured to transfer suction flow442 from input port 424 to suction port 406.

In a step 506, a cyclonic or vortex flow is generated in bothseparators. The first and second separators are configured, as describedherein, to generate a cyclonic or vortex suction flow when a suctionsource is applied to both separators. As applied but not limited tosystem 400, separators 402, 422 are configured to generate from suctionflow 442, a cyclonic flow of matter that is received via input port 404.

In a step 508, an input flow is received at an input port of the firstseparator. As applied but not limited to system 400, input port 404 isconfigured to receive input flow 440. Suction flow 442 has a pressurebelow an ambient air pressure. This pressure difference is configured tocause input flow 440 to flow into input port 404.

In a step 510, liquids and/or solids is separated from the input flow atthe first separator as a suction flow is transmitted from the secondseparator. As applied but not limited to system 400, separator 402 isconfigured to separate suction flow 442 by directing the heavierconstituents (i.e., liquids and solids) of input flow 440 into acyclonic flow pattern that gravity acts upon to cause these heavierconstituents to exit via collection port 408, while the lighterconstituents (i.e., gasses, smoke, aerosols) in input flow 440 arepulled out of separator 402 by the suction at suction port 406. Thus,collection flow 444 includes at least liquids and solids.

In a step 512, liquids and/or solids from the first separator iscollected. For example, as described, a collection port is configured toreceive the heavier constituents and direct them to a canister. Asapplied but not limited to system 400, collection port 408 is configuredto receive the heavier constituents and direct them to collectioncanister 414. Separator 402 is coupled to collection canister 414.Collection canister 414 is configured to receive collection flow 444from collection port 408. Separator 402 is configured to expelcollection flow 444 to collection canister 414 so long as fill volume436 has not reached a predetermined level.

In a step 514 one or more gasses are suctioned through a suction port ofthe first separator. As applied but not limited to system 400, suctionflow 442 may include gasses separated from input flow 440 by separator402. Suction port 406 is configured to pass suction flow 442 fromseparator 402.

In a step 516, the input flow is passed through the suction port of thefirst separator to an input port of the second separator when a firstcanister reaches a predetermined fill volume. As applied but not limitedto system 400, separator 402 is configured to pass input flow 440 fromsuction port 406 to input port 424 unseparated when fill volume 436reaches a predetermined fill volume.

In a step 518, the input flow is received at an input port of a secondseparator. As applied but not limited to system 400, input port 424 isconfigured to receive input flow 440.

In a step 520, liquids and/or solids is separated from the input flow atthe second separator. As applied but not limited to system 400,separator 422 is configured to separate suction flow 442 from collectionflow 444. Suction flow 442 may comprise primarily gasses separated frominput flow 440. Collection flow 444 may comprise primarily liquidsand/or solids separated from input flow 440.

In a step 522, liquids and/or solids are collected from the secondseparator. As applied but not limited to system 400, separator 422 iscoupled to canister 434. Canister 434 is configured to receivecollection flow 444. Collection port 428 is configured to directcollection flow 444 to canister 434. As applied but not limited tosystem 400.

In a step 524, one or more gasses are suctioned through the suction portof the second separator. As applied but not limited to system 400,suction flow 442 may comprise primarily gasses separated from input flow440. Separator 422 is configured to pass suction flow 442 throughsuction port 426.

FIG. 6 is a block diagram illustrating suction system 600. Suctionsystem 600 includes separator 602, collection canister 614, suctionsource 616 and suction attachment 646. Separator 602 is an example ofseparator 100, separator 202, separator 402 and separator 422; however,separator 602 may include alternative configurations and methods ofoperation. Collection canister 614 is an example of collection canister214, collection canister 414 and collection canister 434; however,collection canister 614 may include alternative configurations andmethods of operation. Suction source 616 is an example of suction source416; however, suction source 616 may include alternative configurationsor methods of operation.

In some embodiments, separator 602 includes input port 604, suction port606 and collection port 608.

In some embodiments, input port 604 is integral to a body included aspart of separator 602. Input port 604 may integral to separator 602.Input port 604 is located off-axis from an axis defined by thelongitudinal center of the cylindrical cavity. Input port 604 may beconfigured to direct a flow of matter along the cylindrical cavity wall.By directing the flow of matter along the cylindrical cavity wall,liquids and gasses may cling to the wall of the cavity due to theeffects of centripetal forces. Input port 604 is configured to receive aflow of matter. The flow of matter is pulled into input port 604 by thepressure difference between the ambient air pressure and the lowerpressure provided by suction source 616. In some embodiments, input port604 may include fittings configured to attach tubing. For example,barbed or quick-disconnect type fittings may be used to couple tubing toinput port 604.

Suction port 606 is configured to couple to suction source 616. Incertain embodiments, suction source 616 may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom suction source 616 creates suction at input port 604. Input port604 is configured to receive a flow of matter. The flow of matter ispulled into input port 604 by the pressure difference between theambient air pressure and the lower pressure provided by suction source616. The flow of matter may include liquids, solids, and gasses,including combinations thereof in varying ratios. In some embodiments,input port 604 may include fittings configured to attach tubing. Forexample, barbed or quick-disconnect type fittings may be used to coupletubing to input port 604.

Collection port 608 is configured to expel a collection flow. Thecollection flow may include at least liquids and solids. Collection port608 is disposed at the narrow end of the conical cavity of separator602. Collection port 608 is coupled to collection canister 614.Collection canister 614 may be used to measure the matter collected fromseparator 602. Collection canister 614 may also be used for the safecollection, transportation, and disposal of waste received fromseparator 602. In some embodiments, collection port 608 may include amounting ring configured to form a seal between collection port 608 andcollection canister 614.

Suction attachment 646 is configured to couple to separator 602. Suctionattachment 646 may couple to input port 604 using flexible tubing orpiping to maintain maneuverability of suction attachment 646. In someembodiments, suction attachment 646 may be configured for handheldoperation. In some embodiments, suction attachment 646 may be configuredto couple to a surgical instrument.

In operation, suction source 616 supplies suction to suction port 606.Suction source 616 creates a cyclonic flow within separator 602. Suctionattachment 646 is coupled to input port 604. Input port 604 isconfigured to couple to suction attachment 646. Separator 602 isconfigured to transfer suction from suction source 616 to suctionattachment 646. Suction attachment 646 is configured to receive a flow aflow of matter. The flow of matter is pulled into suction attachment 646by suction source 616. Separator 602 is configured to receive the flowof matter from suction attachment 646 at input port 604. Separator 602is configured to separate liquids and solids from gasses in the flow ofmatter. Collection port 608 is coupled to collection canister 614.Collection port 608 directs a collection flow to collection canister.The collection flow may include at least liquids and solids. A suctionflow is pulled out suction port 606 by suction from suction source 616.The suction flow may comprise primarily gasses. However, in someexamples, the suction flow may comprise liquids, solids and gasses.

FIG. 7 is a diagram illustrating a method of operating a suction system.The steps illustrated in FIG. 7 may be performed by, for example, one ormore elements of suction system 600.

In a step 702, a suction source is applied to a suction port. As appliedbut not limited to system 600, separator 602 includes suction port 606.Suction port 606 is configured to couple to suction source 616. Suctionsource 616 may be configured to apply a suction flow to separator 602.

In a step 704, cyclonic flow is generated in a separator. As applied butnot limited to system 600, separator 602 is configured to generate, froma suction flow, a cyclonic flow of matter that is received via inputport 604.

In a step 706, suction is transferred to a suction attachment. Asapplied but not limited to system 600, separator 602 is configured totransfer suction from suction source 616 to suction attachment 646.

In a step 708, an input flow is received at the suction attachment. Asapplied but not limited to system 600, suction attachment 646 isconfigured to receive an input flow created by suction source 616.

In a step 710, suction flow is adjusted at the suction attachment. Asapplied but not limited to system 600, suction attachment 646 may beconfigured to adjust suction delivered at suction attachment 646.Suction source 616 may be configured to maintain a consistent suctionsupply. Separator 602 continues to function while suction is adjusted bysuction attachment 646.

In a step 712, an input flow is received at an input port. As appliedbut not limited to system 600, input port 604 is coupled to suctionattachment 646. Input port 604 is configured to receive an input flowfrom suction attachment 646.

In a step 714, liquids and solids are separated from the input flow. Asapplied but not limited to system 600, separator 602 is configured toseparate a collection flow from the input flow by directing the heavierconstituents (i.e., liquids and solids) of the input flow into acyclonic flow pattern that gravity acts upon to cause these heavierconstituents to exit via collection port 608, while the lighterconstituents (i.e., gasses, smoke, aerosols) in the input flow arepulled out of separator 602 by the suction at suction port 606.

In a step 716, liquids and solids are directed out of a collection port.As applied but not limited to system 600, collection port 608 isconfigured to receive the heavier constituents and direct them tocollection canister 614. Gases are suctioned through a suction port ofthe separator (718). For example, separator 602 is configured toseparate gasses from the input flow received at input port 604. Suctionsource 616 is configured to suction at least gasses separated from theinput flow from suction port 606.

FIG. 8A is an exploded-view diagram illustrating separator 800.Separator 800 is an example of separator 100, separator 202, separator402, separator 422 and separator 602; however, separator 800 may includealternative configurations and methods of operation.

In some embodiments, separator 800 includes body 802, input port 804,suction port 806, collection port 808, baffle 810, vortex element 812,mounting base 846 and mounting ring 848.

Body 802 includes a cylindrical wall defining a cylindrical cavity. Thecylindrical wall includes a first cylindrical cavity end and a secondcylindrical cavity end. Body 802 also forms a conical cavity. Theconical cavity has a wide end and a narrow end. The wide end is mated tothe second cylindrical cavity end of body 802. In some embodiments, body802 is configured to operate with the first cylindrical cavity end up.Body 802 is configured to allow gravity to pull at least liquid andsolids separated from a flow of matter out collection port 808, whilegasses separated from the flow of matter are pulled by suction out ofsuction port 806.

Input port 804 is configured to receive a flow of matter. The flow ofmatter may be induced into separator 800 via suction port 806 by asuction or vacuum source. Input port 804 is configured to direct a flowof matter along the cylindrical cavity wall. By directing the flow ofmatter along the cylindrical cavity wall, liquids and gasses may clingto the wall of the cavity due to the effects of centripetal forces.Input port 804 is integral to body 802. Input port 804 is disposed inthe cylindrical cavity wall of body 802. Input port 804 is locatedoff-axis from an axis defined by the longitudinal center of thecylindrical cavity.

Suction port 806 is configured to couple to suction source 816. Incertain embodiments, suction source 816 may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom suction source 816 creates suction at input port 804. Input port804 is configured to receive a flow of matter. The flow of matter ispulled into input port 804 by the pressure difference between theambient air pressure and the lower pressure provided by suction source816. The flow of matter may include liquids, solids, and gasses,including combinations thereof in varying ratios. In some embodiments,input port 804 may include fittings configured to attach tubing. Forexample, barbed or quick-disconnect type fittings may be used to coupletubing to input port 804.

Collection port 808 is configured to expel a collection flow. Thecollection flow may comprise at least liquids and solids. Collectionport 808 is disposed at the narrow end of the conical cavity of body802. In an embodiment, collection port 808 may be configured to coupleto a collection canister. A collection canister may be used to measurethe matter collected from separator 800. A collection canister may alsobe used for the safe collection and disposal of waste received fromseparator 800. In some embodiments, collection port 808 may be coupledto tubing or piping to direct matter to a waste drain. In someembodiments, collection port 808 may include mounting ring 848configured to form a seal between collection port 808 to tubing or acollection canister.

Baffle 810 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 804 to suction port 806 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 802. Baffle 810 is disposed betweeninput port 804 and suction port 806. Baffle 810 includes passagewaysconfigured to allow at least gasses in a flow of matter to separate fromliquids and solids that maybe included in the flow. Gasses may be pulledthrough baffle 810 and out suction port 806. Baffle 810 includes a solidsurface located proximal to input port 804 configured to direct the flowto traverse at least a first portion of a circumference of thecylindrical wall of body 802. The solid surface included in baffle 810may to prevent liquids and solids in the flow from being pulled directlyfrom input port 804 to suction port 806 by allowing time for gravity toact on the liquids and solids before they reach an opening in baffle810. By allowing time for gravity to act on the liquids and solids asthey traverse the solid surface of baffle 810, the liquids and solidscan descend towards collection port 808 and thereby not be suctioned outof the suction port 806.

Vortex element 812 is configured to allow a collection flow to passthrough the annular cavity before dropping out collection port 808. Thecollection flow may comprise at least liquids and solids. Vortex element812 includes a cylindrical central member disposed within thecylindrical cavity of body 802. The cylindrical central member forms anannular cavity between vortex element 812 and body 802. Vortex element812 includes a tapered section disposed in the conical cavity of body802. Vortex element 812 includes a plurality of cylindrical sectionshaving different diameters. The plurality of cylindrical sectionsincludes a first section that defines a first portion of the annularcavity and a second section that defines a second portion of the annularcavity. The tapered and cylindrical sections may be configured to directthe flow within body 802 in a cyclonic flow pattern. Baffle 810 isintegral to vortex element 812.

Mounting base 846 is configured to allow separator 800 to be assembled.Mounting base 846 is configured to couple to body 802. Mounting base 846is configured to couple to mounting ring 848.

Mounting ring 848 is configured to operate as a seal for suction port806. Mounting ring 848 may be made from a flexible material that forms aseal between separator 800 and a coupling to a suction source.

FIG. 8B is a diagram illustrating vortex element 800. Vortex element 812is configured to form an annular cavity between vortex element 812 andbody 802. Vortex element 812 is configured to generate a vortex flowwithin body 802. The vortex flow and gravity may cause liquids andsolids in a flow of matter received at input port 804 to separate fromgasses. Vortex element 812 includes a cylindrical central memberdisposed within the generally cylindrical cavity of body 802. Vortexelement 812 includes a tapered section disposed near the conical cavityof body 802. Vortex element 812 includes a plurality of cylindricalsections having different diameters. The plurality of cylindricalsections includes a first section that defines a first portion of theannular cavity and a second section that defines a second portion of theannular cavity. Baffle 810 is integral to vortex element 812.

Vortex element 812 includes baffle 810. Baffle 810 is configured toprevent liquids or solids in the flow from being pulled directly frominput port 804 to suction port 806 without traversing at least a firstportion of a circumference of the cylindrical wall of separator body802. Baffle 810 is disposed between input port 804 and suction port 806.Baffle 810 includes passageways configured to allow at least gasses in aflow of matter to separate from liquids and solids that maybe includedin the flow. Gasses may be pulled through baffle 810 and out suctionport 806. Baffle 810 includes a solid surface located proximal to inputport 804 configured to direct the flow to traverse at least a firstportion of a circumference of the cylindrical wall of body 802. Thesolid surface included in baffle 810 may to prevent liquids and solidsin the flow from being pulled directly from input port 804 to suctionport 806 by allowing time for gravity to act on the liquids and solidsbefore they reach an opening in baffle 810. By allowing time for gravityto act on the liquids and solids as they traverse the solid surface ofbaffle 810, the liquids and solids can descend towards collection port808 and thereby not be suctioned out of the suction port 806.

FIG. 8C is a top-view diagram illustrating the operation of separator800. In operation, a suction source coupled to suction port 806 inducesinput flow 840 within separator 800. Input flow 840 enters separator 800through input port 804. Baffle 810 includes passageways 850 configuredto allow at least gasses to exit separator 800 via collection port 808.Baffle 810 does not include passageways 850 immediately proximal toinput port 804 forcing input flow 840 to traverse at least a firstportion of a circumference of the interior of body 802.

FIG. 8D is a cross-section diagram illustrating the operation ofseparator 800. Separator 800 includes body 802, input port 804, suctionport 806, collection port 808, baffle 810, vortex element 812, mountingbase 846 and mounting ring 848. The elements in FIG. 8D have beenpreviously described.

In operation, a suction supply is coupled to suction port 806. Suctionport 806 is configured to transfer suction from a suction source toinput port 804. Suction from a suction source induces input flow 840 toenter input port 804. Baffle 810 includes passageways 850 configured toallow at least gasses included in input flow 840 to exit separator 800via suction port 806. Baffle 810 includes a solid surface immediatelyproximal to input port 804 forcing input flow 840 to traverse at least afirst portion of the interior of body 802. Vortex element 812 forms anannular opening between vortex element 812 and the interior cavity ofbody 802. A combination of cyclonic flow generated by separator 800 andgravity cause collection flow 844 to separate out of input flow 840.Collection flow 844 may include at least liquids and solids separatedfrom input flow 840. Collection flow 844 is expelled out collection port808. Separator 800 is configured to separate suction flow 842 from inputflow 840. Suction flow 842 is pulled out suction port 806 by a suctionsource.

FIG. 9A is an exploded-view diagram illustrating separator 900.Separator 900 is an example of separator 100, separator 202, separator402, separator 422 and separator 602; however, separator 900 may includealternative configurations and methods of operation.

In some embodiments, separator 900 includes body 902, input port 904,suction port 906, collection port 908, baffle 910, vortex element 912,mounting base 946 and mounting ring 948.

Body 902 includes a cylindrical wall defining a cylindrical cavity. Thecylindrical wall includes a first cylindrical cavity end and a secondcylindrical cavity end. Body 902 also forms a conical cavity. Theconical cavity has a wide end and a narrow end. The wide end is mated tothe second cylindrical cavity end of body 902. In some embodiments, body902 is configured to operate with the first cylindrical cavity end up.Body 902 is configured to allow gravity to pull at least liquid andsolids separated from a flow of matter out collection port 908, whilegasses separated from the flow of matter are pulled by suction out ofsuction port 906.

Input port 904 is configured to receive a flow of matter. The flow ofmatter may be induced into separator 900 via suction port 906 by asuction or vacuum source. Input port 904 is configured to direct a flowof matter along the cylindrical cavity wall of body 902. By directingthe flow of matter along the cylindrical cavity wall, liquids and gassesmay cling to the wall of the cavity due to the effects of centripetalforces. Input port 904 is integral to body 902. Input port 904 isdisposed in the cylindrical cavity wall. Input port 904 is locatedoff-axis from an axis defined by the longitudinal center of thecylindrical cavity.

Suction port 906 is configured to couple to a suction source. In certainembodiments, the suction source may include a vacuum pump, aspirator,and/or a positive pressure operated suction source—such as suctionsources that take advantage of Venturi or Coanda effect. Suction from asuction source is transferred from suction port 906 to input port 904.Input port 904 is configured to receive a flow of matter. The flow ofmatter is pulled into input port 904 by the pressure difference betweenthe ambient air pressure the lower pressure provided by the suctionsource. The flow of matter may include liquids, solids, and gasses,including combinations thereof in varying ratios. Suction port 906 isdisposed near the first cylindrical cavity end. Suction port 906provides suction received from a suction source for operating separator900. In some embodiments, suction port 906 may include fittingsconfigured to attach tubing. For example, barbed or quick-disconnecttype fittings may be used to couple tubing to suction port 906. Thetubing may be used to couple suction port 906 to a suction source or toan input port 904 of another separator.

Collection port 908 is configured to expel a collection flow. Thecollection flow may comprise at least liquids and solids. Collectionport 908 is disposed at the narrow end of the conical cavity of body902. In an embodiment, collection port 908 may be configured to coupleto a collection canister. A collection canister may be used to measurethe matter collected from separator 900. A collection canister may alsobe used for the safe collection, transportation and disposal of wastereceived from separator 900. In some embodiments, collection port 908may be coupled to tubing or piping to direct matter to a waste drain. Insome embodiments, collection port 908 may include a mounting ring 948configured to form a seal between collection port 908 to tubing or acollection canister.

Baffle 910 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 904 to suction port 906 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 902. Baffle 910 is disposed betweeninput port 904 and suction port 906. Baffle 910 includes passageways 950configured to allow at least gasses in a flow of matter to separate fromliquids and solids that maybe included in the flow. Gasses may be pulledthrough baffle 910 and out suction port 906. Baffle 910 includes a solidsurface located proximal to input port 904 configured to direct the flowto traverse at least a first portion of a circumference of thecylindrical wall of body 902. The solid surface included in baffle 910may prevent liquids and solids in the flow from being pulled directlyfrom input port 904 to suction port 906 by allowing time for gravity toact on the liquids and solids before they reach an opening in baffle910. By allowing time for gravity to act on the liquids and solids asthey traverse the solid surface of baffle 910, the liquids and solidscan descend towards collection port 908 and thereby not be suctioned outof the suction port 906.

Vortex element 912 is configured to form an annular cavity betweenvortex element 912 and body 902. Vortex element 912 is configured togenerate a vortex flow within body 902. The vortex flow and gravity maycause liquids and solids in a flow of matter received at input port 904to separate from gasses. Liquids and gases may be expelled outcollection port 908. Vortex element 912 includes a cylindrical centralmember disposed within the generally cylindrical cavity of body 902.Vortex element 912 includes a tapered section disposed near the conicalcavity of body 902. Vortex element 912 includes a plurality ofcylindrical sections having different diameters. The plurality ofcylindrical sections includes a first section that defines a firstportion of the annular cavity and a second section that defines a secondportion of the annular cavity. Baffle 910 is integral to vortex element912.

Mounting base 946 is configured to allow separator 900 to be assembled.Mounting base 946 is configured to couple to body 902. Mounting base 946is configured to couple to mounting ring 948.

Mounting ring 948 is configured to operate as a seal for suction port906. Mounting ring 948 may be made from a flexible material that forms aseal between separator 900 and a coupling to a suction source.

FIG. 9B is a diagram illustrating vortex element 912. Separator 900includes vortex element 912. Vortex element 912 is configured to form anannular cavity between vortex element 912 and body 902. Vortex element912 is configured to generate a vortex flow within body 902. The vortexflow and gravity may cause liquids and solids in a flow of matterreceived at input port 904 to separate from gasses. Liquids and gasesmay be expelled out collection port 908. Vortex element 912 includes acylindrical central member disposed within the generally cylindricalcavity of body 902. Vortex element 912 includes a tapered sectiondisposed near the conical cavity of body 902. Vortex element 912includes a plurality of cylindrical sections having different diameters.The plurality of cylindrical sections includes a first section thatdefines a first portion of the annular cavity and a second section thatdefines a second portion of the annular cavity. Baffle 910 is integralto vortex element 912.

Vortex element 912 includes baffle 910. Baffle 910 is configured toprevent liquids or solids in the flow from being pulled directly frominput port 904 to suction port 906 without traversing at least a firstportion of a circumference of the cylindrical wall of separator body902. Baffle 910 is disposed between input port 904 and suction port 906.Baffle 910 includes passageways 950 configured to allow at least gassesin a flow of matter to separate from liquids and solids that maybeincluded in the flow. Gasses may be pulled through baffle 910 and outsuction port 906. Baffle 910 includes a solid surface located proximalto input port 904 configured to direct the flow to traverse at least afirst portion of a circumference of the cylindrical wall of body 902.The solid surface included in baffle 910 may prevent liquids and solidsin the flow from being pulled directly from input port 904 to suctionport 906 by allowing time for gravity to act on the liquids and solidsbefore they reach an opening in baffle 910. By allowing time for gravityto act on the liquids and solids as they traverse the solid surface ofbaffle 910, the liquids and solids can descend towards collection port908 and thereby not be suctioned out of the suction port 906.

FIG. 9C is a top-view diagram illustrating the operation of separator900. In operation, a suction source coupled to suction port 906 inducesinput flow 940 within separator 900. Input flow 940 enters separator 900through input port 904. Baffle 910 includes passageways 950 configuredto allow at least gasses to exit separator 900 via suction port 906.Baffle 910 does not include passageways 950 immediately proximal toinput port 904 forcing input flow 940 to traverse at least a firstportion of a circumference of the interior of body 902.

FIG. 9D is a cross-section diagram illustrating the operation ofseparator 900. Separator 900 includes body 902, input port 904, suctionport 906, collection port 908, baffle 910, vortex element 912, mountingbase 946 and mounting ring 948. The elements in FIG. 9D have beenpreviously described.

In operation, a suction supply is coupled to suction port 906. Suctionport 906 is configured to transfer suction from a suction source toinput port 904. Suction from a suction source induces input flow 940 toenter input port 904. Baffle 910 includes passageways 950 configured toallow at least gasses included in input flow 940 to exit separator 900via suction port 906. Baffle 910 does not include passageways 950immediately proximal to input port 904 forcing input flow 940 totraverse at least a first portion of the interior of body 902. Vortexelement 912 forms an annular opening between vortex element 912 and theinterior cavity of body 902. A combination of cyclonic flow generated byseparator 900 and gravity cause collection flow 944 to separate out ofinput flow 940. Collection flow 944 may include at least liquids andsolids separated from input flow 940. Collection flow 944 is expelledout collection port 908. Separator 900 is configured to separate suctionflow 942 from input flow 940. Suction flow 942 is pulled out suctionport 906 by a suction source.

FIG. 10A is an exploded-view diagram illustrating separator 1000.Separator 1000 is an example of separator 100, separator 202, separator402, separator 422 and separator 602; however, separator 1000 mayinclude alternative configurations and methods of operation.

In some embodiments, separator 1000 includes body 1002, input port 1004,suction port 1006, collection port 1008, baffle 1010, vortex element1012, mounting base 1046 and mounting ring 1048.

Body 1002 includes a cylindrical wall defining a cylindrical cavity. Thecylindrical wall includes a first cylindrical cavity end and a secondcylindrical cavity end. Body 1002 also forms a conical cavity. Theconical cavity has a wide end and a narrow end. The wide end is mated tothe second cylindrical cavity end of body 1002. In some embodiments,body 1002 is configured to operate with the first cylindrical cavity endup. Body 1002 is configured to allow gravity to pull at least liquid andsolids separated from a flow of matter out collection port 1008, whilegasses separated from the flow of matter are pulled by suction out ofsuction port 1006.

Input port 1004 is configured to receive a flow of matter. The flow ofmatter may be induced into separator 1000 via suction port 1006 by asuction or vacuum source. Input port 1004 is configured to direct a flowof matter along the cylindrical cavity wall. By directing the flow ofmatter along the cylindrical cavity wall, liquids and gasses may clingto the wall of the cavity due to the effects of centripetal forces.Input port 1004 is integral to body 1002. Input port 1004 is disposed inthe cylindrical cavity wall. Input port 1004 is located off-axis from anaxis defined by the longitudinal center of the cylindrical cavity.

Suction port 1006 is configured to couple to a suction source. Incertain embodiments, the suction source may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 1006 to inputport 1004. Input port 1004 is configured to receive a flow of matter.The flow of matter is pulled into input port 1004 by the pressuredifference between the ambient air pressure the lower pressure providedby the suction source. The flow of matter may include liquids, solids,and gasses, including combinations thereof in varying ratios. Suctionport 1406 is disposed near the first cylindrical cavity end. Suctionport 1006 provides suction received from a suction source for operatingseparator 1000. In some embodiments, suction port 1006 may includefittings configured to attach tubing. For example, barbed orquick-disconnect type fittings may be used to couple tubing to suctionport 1006. The tubing may be used to couple suction port 1406 to asuction source or to an input port 1004 of another separator system.

Collection port 1008 is configured to expel a collection flow. Thecollection flow may comprise at least liquids and solids. Collectionport 1008 is disposed at the narrow end of the conical cavity of body1002. In an embodiment, collection port 1008 may be configured to coupleto a collection canister. A collection canister may be used to measurethe matter collected from separator 1000. A collection canister may alsobe used for the safe collection, transportation and disposal of wastereceived from separator 1000. In some embodiments, collection port 1008may be coupled to tubing or piping to direct matter to a waste drain. Insome embodiments, collection port 1008 may include mounting ring 1048configured to form a seal between collection port 1008 to tubing or acollection canister.

Baffle 1010 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 1004 to suction port 1006 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 1002. Baffle 1010 is disposed betweeninput port 1004 and suction port 1006. Baffle 1010 includes passageways1050 configured to allow at least gasses in a flow of matter to separatefrom liquids and solids that maybe included in the flow. Gasses may bepulled through baffle 1010 and out suction port 1006. Baffle 1010includes a solid surface located proximal to input port 1004 configuredto direct the flow to traverse at least a first portion of acircumference of the cylindrical wall of body 1002. The solid surfaceincluded in baffle 1010 may to prevent liquids and solids in the flowfrom being pulled directly from input port 1004 to suction port 1006 byallowing time for gravity to act on the liquids and solids before theyreach an opening in baffle 1010. By allowing time for gravity to act onthe liquids and solids as they traverse the solid surface of baffle1010, the liquids and solids can descend towards collection port 1008and thereby not be suctioned out of the suction port 1006. Baffle 1010is integral to vortex element 1012.

Vortex element 1012 is configured to form an annular cavity betweenvortex element 1012 and body 1002. Vortex element 1012 is configured togenerate a vortex flow within body 1002. The vortex flow and gravity maycause liquids and solids in a flow of matter received at input port 1004to separate from gasses. Liquids and gases may be expelled outcollection port 1008. Vortex element 1012 includes a cylindrical centralmember disposed within the generally cylindrical cavity of body 1002.Vortex element 1012 includes a tapered section disposed near the conicalcavity of body 1002. Vortex element 1012 is integral to baffle 1010.

Mounting base 1046 is configured to allow separator 1000 to beassembled. Mounting base 1046 is configured to couple to body 1002.Mounting base 1046 is configured to couple to mounting ring 1048.

Mounting ring 1048 is configured to operate as a seal for suction port1006. Mounting ring 1048 may be made from a flexible material that formsa seal between separator 1000 and a coupling to a suction source.

FIG. 10B is a diagram illustrating vortex element 1012. Vortex element1012 is configured to form an annular cavity between vortex element 1012and body 1002. Vortex element 1012 is configured to generate a vortexflow within body 1002. The vortex flow and gravity may cause liquids andsolids in a flow of matter received at input port 1004 to separate fromgasses. Liquids and gases may be expelled out collection port 1008.Vortex element 1012 includes a cylindrical central member disposedwithin the generally cylindrical cavity of body 1002. Vortex element1012 includes a tapered section disposed near the conical cavity of body1002. Baffle 1010 is integral to vortex element 1012.

FIG. 10C is a top-view diagram illustrating the operation of separator1000. In operation, a suction source coupled to suction port 1006induces input flow 1040 within separator 1000. Flow 1040 entersseparator 1000 through input port 1004. Baffle 1010 includes passageways1050 configured to allow at least gasses to exit separator 1000 viasuction port 1006. Baffle 1010 does not include passageways 1050immediately proximal to input port 1004 forcing input flow 1040 totraverse at least a first portion of a circumference of the interior ofbody 1002.

FIG. 10D is a cross-section diagram illustrating the operation ofseparator 1000. Separator 1000 includes body 1002, input port 1004,suction port 1006, collection port 1008, baffle 1010, vortex element1012, mounting base 1046 and mounting ring 1048. The elements in FIG.10D have been previously described. FIG. 10D is included for furtherreference.

In operation, a suction supply is coupled to suction port 1006. Suctionport 1006 is configured to transfer suction from a suction source toinput port 1004. Suction from a suction source induces input flow 1040to enter input port 1004. Baffle 1010 includes passageways 1050configured to allow at least gasses included in input flow 1040 to exitseparator 1000 via suction port 1006. Baffle 1010 does not includepassageways 1050 immediately proximal to input port 1004 forcing inputflow 1040 to traverse at least a first portion of the interior of body1002. Vortex element 1012 forms an annular opening between vortexelement 1012 and the interior cavity of body 1002. A combination ofcyclonic flow generated by separator 1000 and gravity cause collectionflow 1044 to separate out of input flow 1040. Collection flow 1044 mayinclude at least liquids and solids separated from input flow 1040.Collection flow 1044 is expelled out collection port 1008. Separator1000 is configured to separate suction flow 1042 from input flow 1040.Suction flow 1042 is pulled out suction port 1006 by a suction source.

FIG. 11A is an exploded-view diagram illustrating separator 1100.Separator 1100 is an example of separator 100, separator 202, separator402, separator 422 and separator 602; however, separator 1100 mayinclude alternative configurations and methods of operation.

In some embodiments, separator 1100 includes body 1102, input port 1104,suction port 1106, collection port 1108, baffle 1110 and vortex element1112.

Body 1102 includes a cylindrical wall defining a cylindrical cavity. Thecylindrical wall includes a first cylindrical cavity end and a secondcylindrical cavity end. Body 1102 also forms a conical cavity. Theconical cavity has a wide end and a narrow end. The wide end is mated tothe second cylindrical cavity end of body 1102. In some embodiments,body 1102 is configured to operate with the first cylindrical cavity endup. Body 1102 is configured to allow gravity to pull at least liquid andsolids separated from a flow of matter out collection port 1108, whilegasses separated from the flow of matter are pulled by suction out ofsuction port 1106.

Input port 1104 is integral to body 1102. Input port 1104 is disposed inthe cylindrical cavity wall. Input port 1104 is located off-axis from anaxis defined by the longitudinal center of the cylindrical cavity. Inputport 1104 is configured to receive a flow of matter. The flow of mattermay be induced into separator 1100 via suction port 1106 by a suction orvacuum source. Input port 1104 is configured to direct a flow of matteralong the cylindrical cavity wall. By directing the flow of matter alongthe cylindrical cavity wall, liquids and gasses may cling to the wall ofthe cavity due to the effects of centripetal forces.

Collection port 1108 is disposed at the narrow end of the conical cavityof body 1102. Collection port 1108 is configured to expel at leastliquids and solids. In an embodiment, collection port 1108 may beconfigured to couple to a collection canister. A collection canister maybe used to measure the matter collected from separator 1100. Acollection canister may also be used for the safe collection,transportation and disposal of waste received from separator 1100. Insome embodiments, collection port 1108 may be coupled to tubing orpiping to direct matter to a waste drain. In some embodiments,collection port 1108 may include a mounting ring configured to form aseal between collection port 1108 to tubing or a collection canister.

Baffle 1110 is disposed between input port 1104 and suction port 1106.Baffle 1110 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 1104 to suction port 1106 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 1102. Baffle 1110 includes a solidsurface located proximal to input port 1104. The solid surface may beused to prevent liquids and solids in the flow from being pulleddirectly from input port 1104 to suction port 1106 by allowing time forgravity to act on the liquids and solids before they reach an opening inbaffle 1110. By allowing time for gravity to act on the liquids andsolids as they traverse the solid surface of baffle 1110, the liquidsand solids can descend towards collection port 1308 and thereby not besuctioned out of the suction port 1106. Baffle 1110 is integral tovortex element 1112.

Vortex element 1112 includes a tapered cylindrical central memberdisposed within the generally cylindrical cavity of body 1102. Vortexelement 1112 is configured to form an annular cavity between vortexelement 1112 and body 1102. Vortex element 1112 is configured togenerate a vortex flow within body 1102. The vortex flow and gravity maycause liquids and solids in a flow of matter received at input port 1104to separate from gasses. Liquids and solids may be expelled outcollection port 1108. Vortex element 1112 includes a lumen disposedwithin the cylindrical central member configured to allow at leastgasses to pass through vortex element 1112 to suction port 1106. Baffle1110 is integral to vortex element 1112.

FIG. 11B is a top-view diagram illustrating the operation of separator1100. In operation, a suction source coupled to suction port 1106induces input flow 1140 within separator 1100. Input flow 1140 entersseparator 1100 through input port 1104. Baffle 1110 includes suctionport 1106 configured to allow at least gasses to exit separator 1100.Baffle 1110 is configured to force input flow 1140 to traverse at leasta first portion of a circumference of the interior of body 1102 beforeexiting suction port 1106.

FIG. 11C is a cross-section diagram illustrating the operation ofseparator 1100. Separator 1100 includes body 1102, input port 1104,suction port 1106, collection port 1108, baffle 1110 and vortex element1112.

In operation, Separator 1100 is configured to separate suction flow 1142from input flow 1140. A suction source is coupled to suction port 1106.Suction port 1106 is configured to transfer suction from a suctionsource to input port 1104. Suction from a suction source induces inputflow 1140 to enter input port 1104. Baffle 1110 is configured to forceinput flow 1140 to traverse at least a first portion of the interior ofbody 1102 before passing out suction port 1106. Vortex element 1112 isconfigured to allow suction flow 11142 separated from input flow 1140 toexit separator 1100 via suction port 1106. Vortex element 1112 forms anannular opening between vortex element 1112 and the interior cavity ofbody 1102. A combination of cyclonic flow generated by separator 1100and gravity may cause collection flow 1144 to separate from input flow1140. Collection flow 1144 may include at least liquids and solidsseparated from input flow 1140. Collection flow 1144 is expelled outcollection port 1108. Suction flow 1142 is pulled out suction port 1106by a suction source.

FIG. 12 is a block diagram illustrating a separator system 1200.Separator 1202 and separator 1222 are examples separator 100, separator202, separator 402, separator 422 and separator 602, separator 800,separator 900, separator 1000, and separator 1100; however, separatorsystem 1200 may include alternative configurations and methods ofoperation.

In some embodiments, separator system 1200 includes separator 1202,canister 1214, separator 1222, input tubing 1230, separator couplingtubing 1232, canister 1234 and output tubing 1236.

In some embodiments, separator 1202 includes input port 1204, suctionport 1206, collection port 1208, baffle 1210 and vortex element 1212.

Separator 1202 includes a body with a cylindrical cavity having acylindrical cavity wall, a first cylindrical cavity end, and a secondcylindrical cavity end. In some embodiments, separator 1202 may beconfigured to operate with the first cylindrical end up. The body mayinclude a conical cavity. The conical cavity may include a wide end anda narrow end. The wide end may be coupled to the second cylindricalcavity end.

In some embodiments, input port 1204 may be integral to a body includedas part of separator 1202. Input port 1204 may integral to separator1202. Input port 1204 maybe located off-axis from an axis defined by thelongitudinal center of separator 1202. Input port 1204 is configured todirect input flow 1240 of matter along the interior of separator 1202.Input port 1204 is configured to receive input flow 1240. Input flow1240 may be induced into separator 1202 via suction source 1216. Suctionport 1206 is configured to couple to suction source 1216. As illustratedin FIG. 12 , suction port 1206 may be configured to receive suction fromsuction source 1216 after the suction has passed through another device,such as separator 1222. In some embodiments, suction source 1216 mayinclude a vacuum pump, aspirator, and/or a positive pressure operatedsuction device that takes advantage of the Coanda effect. In someembodiments, input port 1204 may include fittings configured to attachtubing. For example, barbed or quick-disconnect type fittings may beused to couple tubing to input port 1204.

Suction port 1206 is disposed near a first end of separator 1202.Suction port 1206 is configured to couple to suction source 1216 oranother separator, such as separator 1222. Suction port 1206 providessuction received from suction source 1216 to operate separator 1202. Insome embodiments, suction port 1206 may include fittings configured toattach tubing. For example, barbed or quick-disconnect type fittings maybe used to couple tubing to suction port 1206. The tubing may be used tocouple suction port 1206 to suction source 1216 or to input port 1224 ofseparator 1222.

Collection port 1208 may be disposed at a second end of separator 1202.Collection port 1208 is configured to expel at least liquids and solids.Collection port 1208 is configured to couple to canister 1214. Canister1214 may be used to measure matter collected from separator 1202.Canister 1214 may also be used for the safe collection and disposal ofwaste received from separator 1202. In some embodiments, collection port1208 may be coupled to tubing or piping to direct matter to a wastedrain. In some embodiments, collection port 1208 may include a mountingring configured to form a seal between collection port 1208 and canister1214.

Canister 1214 is configured to receive a collection flow from separator1202. The collection flow may include liquids and solids separated frominput flow 1240 received at input port 1204. The collection flow mayinclude surgical byproducts. Canister 1214 may be used to measure theamount of liquids and/or solids separated from input flow 1240 receivedat input port 1204. Canister 1214 may be configured to permit the safecollection and disposal of waste. In some embodiments, canister 1214 mayinclude a valve configured to activate when canister 1214 is filled to apre-determined volume. The valve may be used to prevent waste fromleaving canister 1214 during transportation. In some embodiments,canister 1214 may include a commercially available collection canister.

Separator system 1200 includes separator 1222 and collection canister1234. Separator 1222 may include similar configurations and methods ofoperation as separator 1202. For the sake of brevity, separator 1222will not be described further. Likewise collection canister 1234 mayinclude similar configurations and methods of operation as canister1214. For the sake of brevity, collection canister 1234 will not bedescribed further.

Suction source 1216 may be any device configured to generate a pressurebelow an ambient air pressure. Suction source 1216 may include a vacuumpump, aspirator or Coanda based positive pressure operated suctiondevice. In some embodiments, suction source 1216 may be configured totake advantage of the Coanda or Venturi effect.

In operation, suction source 1216 supplies a suction flow to suctionport 1226 via output tubing 1236. Separator 1222 is configured totransfer the suction flow to separator 1202. Suction flow 1242 creates apressure near input port 1204 that is below the ambient air pressure.The ambient air pressure overcomes the pressure of the suction flowthereby inducing input flow 1240 into input port 1204. Input port 1204is configured to receive input flow 1240. Input flow 1240 may compriseliquids, gasses and solids, including combinations thereof in varyingratios. Input flow 1240 may include surgical byproducts. Separator 1202creates a cyclonic flow from the suction flow. The cyclonic flow andgravity cause a collection flow to separate from input flow 1240. Thecollection flow may comprise at least liquids and solids. The collectionflow is expelled from collection port 1208. Collection port 1208 isconfigured to direct the collection flow to collection canister 1214.

Separator 1202 separates a suction flow from a collection flow. In afirst mode of operation, the suction flow may comprise primarily gassesseparated from input flow 1240. The suction flow is pulled fromseparator 1202 by suction source 1216. The suction flow is passed fromsuction port 1206 to input port 1224. Separator 1202 continues tooperate in the first mode of operation until a fill volume withincollection canister 1214 reaches a predetermined volume.

Separators 1202, 1222 may be configured to pass input flow 1240 frominput ports 1204, 1224 to suction ports 1206, 1226 unseparated whencollection canisters 1214, 1234 reach predetermined fill volumes. In asecond mode of operation, separator 1202 may pass input flow 1240through suction port 1206 to separator 1222 unseparated.

In operation, suction source 1216 supplies a suction flow from suctionsource 1216 to suction port 1226. Separator 1222 is configured to passthe suction flow to separator 1202. The suction flow pulls input flow1240 into input port 1204. Separator 1202 passes input flow 1240 frominput port 1204 to suction port 1206 unseparated because a predeterminedfill volume within collection canister 1214 has been reached. Input flow1240 is received by input port 1224. A fill volume in collectioncanister 1234 has not reached a predetermined fill volume. Separator1222 separates a collection flow from a suction flow. The collectionflow may comprise primarily liquids and solids from input flow 1240.Separator 1222 separates a suction flow from a collection flow. Thecollection flow is expelled out collection port 1228. Collection port1228 is coupled to collection canister 1234. Collection canister 1234 isconfigured to receive a collection flow from collection port 1228. Asuction flow is pulled out suction port 1226 by suction source 1216.

FIG. 13A is a block diagram illustrating separator with filter 1300.Separator with filter 1300 is an example of separator 100, separator202, separator 402 and separator 602; however, separator with filter1300 includes electric filter 1352. In addition, separator with filter1300 may include alternative configurations and methods of operationthan the previously described embodiments.

Separator with filter 1300 includes separator body 1302, input port1304, suction port 1306, collection port 1308, baffle 1310, vortexelement 1312 and electric filter 1352 and filter controller 1354. Inoperation, separator 1300 is configured to separate liquids, solids andgasses in a flow of matter. Separator 1300 ejects liquids and solidsseparated from the flow of matter out collection port 1308 whilesuctioning at least gasses separated from the flow of matter out suctionport 1306. Separator 1300 is operated by suction received from a suctionsource. Separator with filter 1300 is further configured to filterparticles from gasses suction from suction port 1306.

Separator with filter 1300 includes separator body 1302. Separator body1302 includes a cylindrical wall defining a cylindrical cavity. Thecylindrical wall includes a first cylindrical cavity end and a secondcylindrical cavity end. Separator body 1302 also forms a conical cavity.The conical cavity has a wide end and a narrow end. The wide end ismated to the second cylindrical cavity end of separator body 1302. Insome embodiments, separator body 1302 is configured to operate with thefirst cylindrical cavity end up. Separator body 1302 is configured toallow gravity to pull at least liquid and solids separated from a flowof matter out collection port 1308, while gasses separated from the flowof matter are pulled by suction out of suction port 1306.

Separator with filter 1300 includes input port 1304. Input port 1304 isconfigured to receive a flow of matter. In some embodiments, input port1304 may be integral to separator body 1302. Input port 1304 may bedisposed in the cylindrical cavity wall. Input port 1304 may be locatedoff-axis from an axis defined by the longitudinal center of thecylindrical cavity. Input port 1304 may be configured to direct a flowof matter along the cylindrical cavity wall. By directing the flow ofmatter along the cylindrical cavity wall, liquids and gasses may clingto the wall of the cavity due to the effects of centripetal forces. Theflow of matter may be induced into separator 1300 by suction receivedfrom suction port 1306 by a suction or vacuum source.

Separator with filter 1300 includes suction port 1306. Suction port 1306is configured to couple to a suction source. In certain embodiments, thesuction source may include a vacuum pump, aspirator, and/or a positivepressure operated suction source—such as suction sources that takeadvantage of Venturi or Coanda effect. Suction from a suction source istransferred from suction port 1306 to input port 1304. Input port 1304is configured to receive a flow of matter. The flow of matter is pulledinto input port 1304 by the pressure difference between the ambient airpressure the lower pressure provided by the suction source. The flow ofmatter may include liquids, solids, and gasses, including combinationsthereof in varying ratios. Suction port 1306 is disposed near the firstcylindrical cavity end. Suction port 1306 provides suction received froma suction source for operating separator canister with filter 1300. Insome embodiments, suction port 1306 may include fittings configured toattach tubing. For example, barbed or quick-disconnect type fittings maybe used to couple tubing to suction port 1306. The tubing may be used tocouple suction port 1306 to a suction source or to an input port 1304 ofanother separator system. Separator 1300 includes collection port 1308.Collection port 1308 is configured to expel at least liquids and solids.Collection port 1308 is disposed at the narrow end of the conical cavityof separator body 1302. In an embodiment, collection port 1308 may beconfigured to couple to a collection canister. A collection canister maybe used to measure the matter collected from separator 1300. Acollection canister may also be used for the safe collection,transportation and disposal of waste received from separator with filter1300. In some embodiments, collection port 1308 may be coupled to tubingor piping to direct matter to a waste drain. In some embodiments,collection port 1308 may include a mounting ring configured to form aseal between collection port 1308 to tubing or a collection canister.Separator with filter 1300 includes baffle 1310. Baffle 1310 is disposedbetween input port 1304 and suction port 1306. Baffle 1310 is configuredto prevent liquids or solids in the flow from being pulled directly frominput port 1304 to suction port 1306 without traversing at least a firstportion of a circumference of the cylindrical wall of separator body1302. In some embodiments, baffle 1310 may include openings configuredto allow at least gasses in a flow of matter to separate from liquidsand solids that maybe included in the flow. Gasses may be pulled throughbaffle 1310 and out suction port 1306. In an embodiment, baffle 1310 mayinclude a solid surface located proximal to input port 1304. The solidsurface that may be included in baffle 1310 may be used to preventliquids and solids in the flow from being pulled directly from inputport 1304 to suction port 1306 by allowing time for gravity to act onthe liquids and solids before they reach an opening in baffle 1310. Byallowing time for gravity to act on the liquids and solids as theytraverse the solid surface of baffle 1310, the liquids and solids candescend towards collection port 1308 and thereby not be suctioned out ofthe suction port 1306.

Separator with filter 1300 includes vortex element 1312. Vortex element1312 is configured to direct a flow of matter in a cyclonic flow. Thecyclonic flow and gravity may cause liquids, solids and gasses includedin the flow of matter to separate. Vortex element 1312 includes acylindrical central member disposed within the cylindrical cavity ofseparator body 1302. The cylindrical central member forms an annularcavity between vortex element 1312 and separator body 1302. Vortexelement 1312 is configured to allow liquids and solids in the flow topass through the annular cavity before dropping out collection port1308. In an embodiment, vortex element 1312 may include a taperedsection disposed in the conical cavity of separator body 1302. In anembodiment, vortex element 1312 may include a plurality of cylindricalsections having different diameters. The plurality of cylindricalsections may include a first section that defines a first portion of theannular cavity and a second section that defines a second portion of theannular cavity. The tapered and cylindrical sections may be configuredto direct the flow within separator body 1302 in a cyclonic flowpattern. In an embodiment, baffle 1310 may be integral to vortex element1312.

Separator with filter 1300 includes electric filter 1352. Electricfilter 1352 is configured to use electrical charge to capture particlesthat may be included in a flow exiting suction port 1306. Electricfilter 1352 may comprise a matrix of conductive elements. In someembodiments, the conductive elements may be iron, steel, copper or someother conductive element. In some embodiments, the matrix may becomprised of stacked screens. In some embodiments, the matrix may becomprised of entwined wire. Electric filter 13552 is coupled to filtercontroller 1354. Electric filter 1352 is configured to receive powerfrom filter controller 1354.

Separator with filter 1300 includes filter controller 1354. Filtercontroller 1354 is configured to operate electric filter 1352 in such amanner as to collect particles included in a flow of matter using anelectrical charge. Filter controller 1354 is configured to provideelectric filter 1352 power at a particular voltage level, current leveland possibly frequency. In some embodiments, filter controller 1354 maybe configured to provide direct current. In some embodiments, filtercontroller may include a microcontroller configured to power electricfilter 1352.

FIG. 13B is a block diagram illustrating separator with filter 1300. Inthis embodiment, separator with filter 1300 includes biological filter1356 rather than electric filter 1352.

Biological filter 1356 is configured to trap biological elementspossibly included in a flow to be expelled from suction port 1306.Various embodiments of filter 1352 may be configured to trap specifictypes of biological elements using different operations.

Biological filter 1356 is disposed within separator body 1302.Biological filter 1356 includes one or more filter inlet ports and oneor more filter output ports. The one or more filter inlet ports areconfigured to receive a flow of matter from baffle 1310. Elementscomprising biological filter 1356 are configured to trap biologicalelements possibly contained in the flow of matter and passes a filtrateto suction port 1306.

Biological filter 1356 may comprise mechanical, biological, chemical orother types of filters including any combination thereof to trapbiological elements. Mechanical filtration may include physical barrieror filter media type filters including combinations thereof

Filters using a physical barrier or filter media retain biologicalelements by physically blocking the biological elements from passingthrough the filter media. Filter media mechanically or physicallystrains biological elements from the effluent passing through it. Filtermedia is available in a variety of materials and porosities, which maybe selected to limit the size of biological elements they can extract.Combinations of different materials and porosities of filter media maybe used to separate specific elements comprising an effluent of thecollected matter and the gasses received via input port 11304 outsuction port 1306.

Biological filter 1356 may be configured to use living microorganisms,such as bacteria and fungi, to capture and biologically degradepollutants, harmful chemicals and other undesirable content from aneffluent. Biological filtration can be used with gases and liquids.Biological filters comprise a filter media on which beneficialmicroorganisms grow. Biological filter media can be made from sand,plastic, metals, ceramics and other materials. Materials having a largesurface area to volume ratio typically provide the best performance inbiological filters.

Biological filter 1356 may be configured to use chemical filtrationmedia to removes dissolved particulates from an effluent via activatedcarbons, resins, and other adsorbents. Chemical filtration media causesunwanted dissolved matter to adhere to it. Two popular forms of chemicalmedia include activated carbon and resins. Activated carbon hasmicroscopic pores that allow certain organic or inorganic materials tostick to them. Carbon removes many harmful elements from an effluent.Ion exchange resins work by attracting a specific molecule to adhere tothem. Resins can be combined with carbon. The resins often strengthenthe filtering ability of the carbon. Protein foam skimming or oxidationwith ozone may also be used for chemical filtration.

FIG. 13C is a block diagram illustrating separator with filter 1300.Separator with filter 1300 is an embodiment of separator with filter1300 which includes electric filter 1352 and biological filter 1356. Theelements included in FIG. 13C have been previously described in FIGS.13A and 13B. For the sake of brevity, these elements will not bediscussed further.

The system may comprise one of more filters. In some embodiments, theone or more filters is positioned within a surgical instrument, within aseparator, between a surgical instrument and a separator, within asuction source, between a separator and a suction source, within afiltration unit, between a separator and a filtration unit, within acanister, between a separator and a canister, or any combinationthereof. In some embodiments, the one or more filters may collect one ormore solids. In some embodiments, the one or more filters may sample aportion of a flow of matter than comprises solids. In some embodiments,the one or more filters may substantially remove an entire portion ofsolids from a flow of matter. In some embodiments, the one or morefilters may remove a portion, such as about 60%, 70%, 80% 90%, 95% ormore, of solids from a flow of matter. In some embodiments, the one ormore filters may separate solids by size. In some embodiments, the oneor more filters may remove solids of a particular size from the flow ofmatter. In some embodiments, the one or more solids collected on the oneor more filters are analyzed in a diagnostic laboratory. In someembodiments, the one or more solids is a bacterium, a bacterialfragment, a bacterial particle, a virus, a viral fragment, a viralparticle, a cell, a cell fragment, a tissue fragment, a non-biologicalmaterial such as polymeric fragments or metallic fragments, or anycombination thereof.

In some embodiments, a pore size of the one or more filters is less thanabout 500, 450, 400, 350, 300, 250, 200, 150, 100, 90, 80, 70, 60, 50,40, 30, 20, 10, 9, 8, 7, 6, 5, 4, 3, 2, 1, 0.5, 0.25 microns or less. Insome embodiments, a pore size of one or more filters is less than about500 microns. In some embodiments, a pore size of one or more filters isless than about 400 microns. In some embodiments, a pore size of one ormore filters is less than about 300 microns. In some embodiments, a poresize of one or more filters is less than about 200 microns. In someembodiments, a pore size of one or more filters is less than about 100microns. In some embodiments, a pore size of one or more filters is lessthan about 75 microns. In some embodiments, a pore size of one or morefilters is less than about 50 microns. In some embodiments, a pore sizeof one or more filters is less than about 25 microns. In someembodiments, a pore size of one or more filters is less than about 10microns. In some embodiments, a pore size of one or more filters is lessthan about 5 microns. In some embodiments, a pore size of one or morefilters is less than about 1 micron. In some embodiments, a pore size ofone or more filters is less than about 0.5 micron. In some embodiments,a pore size of one or more filters is less than about 0.25 micron.

The system may comprise one or more charged matrices, such as one ormore positively charged matrices, one or more negatively chargedmatrices, or any combination thereof. The one or more charged matricesare operatively coupled to the surgical instrument, the separator, thesuction source, or any combination thereof. The one or more chargedmatrices are operative coupled to a suction port of the separator. Theone or more charged matrices may surround a portion of the suction portor a portion of the tubing operatively coupled to the suction port, suchas 25%, 50%, 75%, 90% or more surrounded.

The one or more positively charged matrices is hydrogen, sodium,potassium, lithium, rubidium, cesium, copper, silver, ammonium, calcium,barium, magnesium, zinc, iron, cobalt, manganese, aluminum, or anycombination thereof. The one or more positively charged matrices areFe2+ or Fe3+ or a combination thereof. The one or more negativelycharged matrices is chloride, bromide, iodide, hydroxide, nitrate,nitrite, hydrogencarbonate, hydrogensulphate, sulphate, sulphite,sulphide, oxide, carbonate, copper, phosphate, or any combinationthereof.

FIG. 14 is a block diagram illustrating separator canister system 1400.In operation, separator canister system 1400 is configured to separateliquids, solids and gasses in a flow of matter. Separator canistersystem 1400 ejects liquids and solids separated from the flow of matterout collection port 1408 while suctioning at least gasses separated fromthe flow of matter out suction port 1406. Separator canister system 1400is operated by suction received from a suction source. It should beunderstood that the terms “suction” and “vacuum” as used herein refer toa pressure below the surrounding ambient air pressure.

In some embodiments, separator canister system 1400 includes separatorbody 1402, input port 1404, suction port 1406, collection port 1408,baffle 1410, vortex element 1412 and collection canister 1414.

Separator body 1402 includes a cylindrical wall defining a cylindricalcavity. The cylindrical wall includes a first cylindrical cavity end anda second cylindrical cavity end. Separator body 1402 also forms aconical cavity. The conical cavity has a wide end and a narrow end. Thewide end is mated to the second cylindrical cavity end of separator body1402. In some embodiments, separator body 1402 is configured to operatewith the first cylindrical cavity end up. Separator body 1402 isconfigured to allow gravity to pull at least liquid and solids separatedfrom a flow of matter out collection port 1408, while gasses separatedfrom the flow of matter are pulled by suction out of suction port 1406.

Separator body 1402 is configured to be integrated with collectioncanister 1414. Collection canister 1414 may represent a canister or alid for a canister. In some embodiments, separator body 1402 may beintegrated into the interior of collection canister 1414. In someembodiments, separator body 1402 may be integrated into a lid forcollection canister 1414. In some embodiments, separator body 1402 andcollection canister 1414 may be a single article of manufacture. In someembodiments, separator body 1402 may be configured to couple to canister1414. For some forms of manufacturing, it may be desirable tomanufacture separator body 1402 from a different process than used forcollection canister 1414 and integrate the separator body 1402 andcollection canister 1414 as part of an assembly process.

Input port 1404 is configured to receive a flow of matter. In someembodiments, input port 1404 may be integral to separator body 1402.Input port 1404 may be disposed in the cylindrical cavity wall. Inputport 1404 may be located off-axis from an axis defined by thelongitudinal center of the cylindrical cavity. Input port 1404 may beconfigured to direct a flow of matter along the cylindrical cavity wall.By directing the flow of matter along the cylindrical cavity wall,liquids and gasses may cling to the wall of the cavity due to theeffects of centripetal forces. The flow of matter may be induced intoseparator canister system 1400 by suction received from suction port1406 by a suction or vacuum source.

Suction port 1406 is configured to couple to a suction source. Incertain embodiments, the suction source may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 1406 to inputport 1404. Input port 1404 is configured to receive a flow of matter.The flow of matter is pulled into input port 1404 by the pressuredifference between the ambient air pressure the lower pressure providedby the suction source. The flow of matter may include liquids, solids,and gasses, including combinations thereof in varying ratios. Suctionport 1406 is disposed near the first cylindrical cavity end. Suctionport 1406 provides suction received from a suction source for operatingseparator canister system 1400. In some embodiments, suction port 1406may include fittings configured to attach tubing. For example, barbed orquick-disconnect type fittings may be used to couple tubing to suctionport 1406. The tubing may be used to couple suction port 1406 to asuction source or to an input port 1404 of another separator system.

Collection port 1408 is configured to expel at least liquids and solids.Collection port 1408 is disposed at the narrow end of the conical cavityof separator body 1402. Collection port 1408 is configured to expel atleast liquids and solids into collection canister 1414. Collectioncanister 1414 may be used to measure the matter collected from separatorcanister system 1400. Collection canister 1414 may also be used for thesafe collection, transportation and disposal of waste received fromcollection port 1408.

Baffle 1410 is disposed between input port 1404 and suction port 1406.Baffle 1410 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 1404 to suction port 1406 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 1402. In some embodiments, baffle1410 may include openings configured to allow at least gasses in a flowof matter to separate from liquids and solids that maybe included in theflow. Gasses may be pulled through baffle 1410 and out suction port1406. In an embodiment, baffle 1410 may include a solid surface locatedproximal to input port 1404. The solid surface that may be included inbaffle 1410 may be used to prevent liquids and solids in the flow frombeing pulled directly from input port 1404 to suction port 1406 byallowing time for gravity to act on the liquids and solids before theyreach an opening in baffle 1410. By allowing time for gravity to act onthe liquids and solids as they traverse the solid surface of baffle1410, the liquids and solids can descend towards collection port 108 andthereby not be suctioned out of the suction port 1406.

Vortex element 1412 is configured to direct a flow of matter in acyclonic flow. The cyclonic flow and gravity may cause liquids, solidsand gasses included in the flow of matter to separate. Vortex element1412 includes a cylindrical central member disposed within thecylindrical cavity of separator body 1402. The cylindrical centralmember forms an annular cavity between vortex element 1412 and separatorbody 1402. Vortex element 1412 is configured to allow liquids and solidsin the flow to pass through the annular cavity before dropping outcollection port 1408. In an embodiment, vortex element 1412 may includea tapered section disposed in the conical cavity of separator body 1402.In an embodiment, vortex element 1412 may include a plurality ofcylindrical sections having different diameters. The plurality ofcylindrical sections may include a first section that defines a firstportion of the annular cavity and a second section that defines a secondportion of the annular cavity. The tapered and cylindrical sections maybe configured to direct the flow within separator body 1402 in acyclonic flow pattern. In an embodiment, baffle 1410 may be integral tovortex element 1412. In an embodiment, vortex element 1412 may include alumen disposed within the cylindrical central member configured to allowat least gasses to pass through vortex element 1412 to suction port1406.

Collection canister 1414 represents any portion of a collectioncanister. For example, collection canister 1414 may be a canister,canister wall, a lid or some other portion of a collection canister.Collection canister 1414 is configured to receive matter from collectionport 1408. Collection canister 1414 may be used to measure the volume ofmatter received from collection port 1408. Collection canister 1414 maybe used for the safe collection, transportation and disposal ofcollected waste.

FIG. 15 is a block diagram illustrating separator 1500. In operation,separator 1500 is configured to separate liquids, solids and gasses in aflow of matter. Separator 1500 ejects liquids and solids separated fromthe flow of matter out collection port 1508 while suctioning at leastgasses separated from the flow of matter out suction port 1506.Separator 1500 is operated by suction received from a suction source. Itshould be understood that the terms “suction” and “vacuum” as usedherein refer to a pressure below the surrounding ambient air pressure.

In some embodiments, separator 1500 includes separator body 1502, inputport 1504, suction port 1506, collection port 1508, baffle 1510 andvortex element 1512.

Separator body 1502 includes a cylindrical wall defining a cylindricalcavity. The cylindrical wall includes a first cylindrical cavity end anda second cylindrical cavity end. Separator body 1502 also forms aconical cavity. The conical cavity has a wide end and a narrow end. Thewide end is mated to the second cylindrical cavity end of separator body1502. In some embodiments, separator body 1502 is configured to operatewith the first cylindrical cavity end up. Separator body 1502 isconfigured to allow gravity to pull at least liquid and solids separatedfrom a flow of matter out collection port 1508, while gasses separatedfrom the flow of matter are pulled by suction out of suction port 1506.

Input port 1504 is configured to receive a flow of matter. In someembodiments, input port 1504 may be integral to separator body 1502.Input port 1504 may be disposed in the cylindrical cavity wall. Inputport 1504 may be located off-axis from an axis defined by thelongitudinal center of the cylindrical cavity. Input port 1504 may beconfigured to direct a flow of matter along the cylindrical cavity wall.By directing the flow of matter along the cylindrical cavity wall,liquids and gasses may cling to the wall of the cavity due to theeffects of centripetal forces. The flow of matter may be induced intoseparator 1500 by suction received from suction port 1506 by a suctionor vacuum source.

Input port 1504 includes angle 1560. Angle 1560 represents an anglebetween a longitudinal axis located at the center in input port 1504 anda longitudinal axis located at the center of separator body 1502. Insome embodiments, angle 1560 may equal 90°. In some embodiments, angle1560 may be an acute angle. When angle 1560 is an acute angle, a flow ofmatter entering input port 1504 is directed away from baffle 1510 andtowards collection port 1508. Angle 1560 may improve the operatingefficiency of separator 1500 by directing the flow of matter. Angle 1560may prevent liquids and solids from exiting suction port 1506 withoutfirst traversing at least a portion of an inner circumference ofseparator body 1502.

Suction port 1506 is configured to couple to a suction source. Incertain embodiments, the suction source may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 1506 to inputport 1504. Input port 1504 is configured to receive a flow of matter.The flow of matter is pulled into input port 1504 by the pressuredifference between the ambient air pressure the lower pressure providedby the suction source. The flow of matter may include liquids, solids,and gasses, including combinations thereof in varying ratios. Suctionport 1506 is disposed near the first cylindrical cavity end. Suctionport 1506 provides suction received from a suction source for operatingseparator 1500. In some embodiments, suction port 1506 may includefittings configured to attach tubing. For example, barbed orquick-disconnect type fittings may be used to couple tubing to suctionport 1506. The tubing may be used to couple suction port 1506 to asuction source or to an input port 1504 of another separator system.

Collection port 1508 is configured to expel at least liquids and solids.Collection port 1508 is disposed at the narrow end of the conical cavityof separator body 1502. In an embodiment, collection port 1508 may beconfigured to couple to a collection canister. A collection canister maybe used to measure the matter collected from separator 1500. Acollection canister may also be used for the safe collection,transportation and disposal of waste received from separator 1500. Insome embodiments, collection port 1508 may be coupled to tubing orpiping to direct matter to a waste drain. In some embodiments,collection port 1508 may include a mounting ring configured to form aseal between collection port 1508 to tubing or a collection canister.

Baffle 1510 is disposed between input port 1504 and suction port 1506.Baffle 1510 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 1504 to suction port 1506 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 1502. In some embodiments, baffle1510 may include openings configured to allow at least gasses in a flowof matter to separate from liquids and solids that maybe included in theflow. Gasses may be pulled through baffle 1510 and out suction port1506. In an embodiment, baffle 1510 may include a solid surface locatedproximal to input port 1504. The solid surface that may be included inbaffle 1510 may be used to prevent liquids and solids in the flow frombeing pulled directly from input port 1504 to suction port 1506 byallowing time for gravity to act on the liquids and solids before theyreach an opening in baffle 1510. By allowing time for gravity to act onthe liquids and solids as they traverse the solid surface of baffle1510, the liquids and solids can descend towards collection port 1508and thereby not be suctioned out of the suction port 1506.

Vortex element 1512 is configured to direct a flow of matter in acyclonic flow. The cyclonic flow and gravity may cause liquids, solidsand gasses included in the flow of matter to separate. Vortex element1512 includes a cylindrical central member disposed within thecylindrical cavity of separator body 1502. The cylindrical centralmember forms an annular cavity between vortex element 1512 and separatorbody 1502. Vortex element 1512 is configured to allow liquids and solidsin the flow to pass through the annular cavity before dropping outcollection port 1508. In an embodiment, vortex element 1512 may includea tapered section disposed in the conical cavity of separator body 1502.In an embodiment, vortex element 1512 may include a plurality ofcylindrical sections having different diameters. The plurality ofcylindrical sections may include a first section that defines a firstportion of the annular cavity and a second section that defines a secondportion of the annular cavity. The tapered and cylindrical sections maybe configured to direct the flow within separator body 1502 in acyclonic flow pattern. In an embodiment, baffle 1510 may be integral tovortex element 1512. In some embodiments, vortex element 1512 mayinclude a lumen disposed in the cylindrical central member configured toallow at least gasses to pass through vortex element 1512 to suctionport 1506.

FIG. 16 is a block diagram illustrating separator 1600. In operation,separator 1600 is configured to separate liquids, solids and gasses in aflow of matter. Separator 1600 ejects liquids and solids separated fromthe flow of matter out collection port 1608 while suctioning at leastgasses separated from the flow of matter out suction port 1606.Separator 1600 is operated by suction received from a suction source. Itshould be understood that the terms “suction” and “vacuum” as usedherein refer to a pressure below the surrounding ambient air pressure.

In some embodiments, separator 1600 includes separator body 1602, inputport 1604, suction port 1606, collection port 1608, helical baffle 1610and vortex element 1612.

Separator body 1602 includes a cylindrical wall defining a cylindricalcavity. The cylindrical wall includes a first cylindrical cavity end anda second cylindrical cavity end. Separator body 1602 also forms aconical cavity. The conical cavity has a wide end and a narrow end. Thewide end is mated to the second cylindrical cavity end of separator body1602. In some embodiments, separator body 1602 is configured to operatewith the first cylindrical cavity end up. Separator body 1602 isconfigured to allow gravity to pull at least liquid and solids separatedfrom a flow of matter out collection port 1608, while gasses separatedfrom the flow of matter are pulled by suction out of suction port 1606.

Input port 1604 is configured to receive a flow of matter. In someembodiments, input port 1604 may be integral to separator body 1602.Input port 1604 may be disposed in the cylindrical cavity wall. Inputport 1604 may be located off-axis from an axis defined by thelongitudinal center of the cylindrical cavity. Input port 1604 may beconfigured to direct a flow of matter along the cylindrical cavity wall.By directing the flow of matter along the cylindrical cavity wall,liquids and gasses may cling to the wall of the cavity due to theeffects of centripetal forces. The flow of matter may be induced intoseparator 1600 by suction received from suction port 1606 by a suctionor vacuum source.

Suction port 1606 is configured to couple to a suction source. Incertain embodiments, the suction source may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 1606 to inputport 1604. Input port 1604 is configured to receive a flow of matter.The flow of matter is pulled into input port 1604 by the pressuredifference between the ambient air pressure the lower pressure providedby the suction source. The flow of matter may include liquids, solids,and gasses, including combinations thereof in varying ratios. Suctionport 1606 is disposed near the first cylindrical cavity end. Suctionport 1606 provides suction received from a suction source for operatingseparator 1600. In some embodiments, suction port 1606 may includefittings configured to attach tubing. For example, barbed orquick-disconnect type fittings may be used to couple tubing to suctionport 1606. The tubing may be used to couple suction port 1606 to asuction source or to an input port 1604 of another separator system.

Collection port 1608 is configured to expel at least liquids and solids.Collection port 1608 is disposed at the narrow end of the conical cavityof separator body 1602. In an embodiment, collection port 1608 may beconfigured to couple to a collection canister. A collection canister maybe used to measure the matter collected from separator 1600. Acollection canister may also be used for the safe collection,transportation and disposal of waste received from separator 1600. Insome embodiments, collection port 1608 may be coupled to tubing orpiping to direct matter to a waste drain. In some embodiments,collection port 1608 may include a mounting ring configured to form aseal between collection port 1608 to tubing or a collection canister.

Helical baffle 1610 is disposed between input port 1604 and suction port1606.

Helical baffle 1610 is configured to prevent liquids or solids in theflow from being pulled directly from input port 1604 to suction port1606 without traversing at least a first portion of a circumference ofthe cylindrical wall of separator body 1602. Helical baffle 1610includes a helical portion with a start point near input port 1604 andan end point below input port 1604. The helical portion of helicalbaffle 1610 prevents a flow of matter traveling within separator body1602 from intersecting with a flow of matter entering input port 1604.Helical baffle 1610 may include a second baffle disposed above inputport 1604. In some embodiments, the second baffle may include openingsconfigured to allow at least gasses in a flow of matter to separate fromliquids and solids that maybe included in the flow. In an embodiment,the second baffle may include a solid surface located proximal to inputport 1604. The solid surface that may be included in the second bafflemay be used to prevent liquids and solids in the flow from being pulleddirectly from input port 1604 to suction port 1606 by allowing time forgravity to act on the liquids and solids before they reach an opening inthe second baffle. By allowing time for gravity to act on the liquidsand solids as they traverse the solid surface of the second baffle, theliquids and solids can descend towards collection port 1608 and therebynot be suctioned out of the suction port 1606.

Vortex element 1612 is configured to direct a flow of matter in acyclonic flow. The cyclonic flow and gravity may cause liquids, solidsand gasses included in the flow of matter to separate. Vortex element1612 includes a cylindrical central member disposed within thecylindrical cavity of separator body 1602. The cylindrical centralmember forms an annular cavity between vortex element 1612 and separatorbody 1602. Vortex element 1612 is configured to allow liquids and solidsin the flow to pass through the annular cavity before dropping outcollection port 1608. In an embodiment, vortex element 1612 may includea tapered section disposed in the conical cavity of separator body 1602.In an embodiment, vortex element 1612 may include a plurality ofcylindrical sections having different diameters. The plurality ofcylindrical sections may include a first section that defines a firstportion of the annular cavity and a second section that defines a secondportion of the annular cavity. The tapered and cylindrical sections maybe configured to direct the flow within separator body 1602 in acyclonic flow pattern. In an embodiment, baffle 1610 may be integral tovortex element 1612. In some embodiments, vortex element 1612 mayinclude a lumen passing through the center configured to allow at leastgasses to be evacuated via suction port 1606. In an embodiment, vortexelement 1612 may include a lumen disposed within the cylindrical centralmember configured to allow at least gasses to pass through vortexelement 1612 to suction port 1606.

FIG. 17 is a block diagram illustrating separator system 1700. Inoperation, separator system 1700 is configured to separate liquids,solids and gasses in a flow of matter. Separator system 1700 ejectsliquids and solids separated from the flow of matter out collection port1708 while suctioning at least gasses separated from the flow of matterout suction port 1706. Tissue trap 1762 is configured to collect solidsthat may be included in a flow received from collection port 1706.Tissue trap 1762 is configured to allow liquids to pass through tocollection canister 1714. Separator system 1700 is operated by suctionreceived from a suction source. It should be understood that the terms“suction” and “vacuum” as used herein refer to a pressure below thesurrounding ambient air pressure.

In some embodiments, separator system 1700 includes separator body 1702,input port 1704, suction port 1706, collection port 1708, baffle 1710,vortex element 1712, collection canister 1714 and tissue trap 1762.

Separator body 1702 includes a cylindrical wall defining a cylindricalcavity. The cylindrical wall includes a first cylindrical cavity end anda second cylindrical cavity end. Separator body 1702 also forms aconical cavity. The conical cavity has a wide end and a narrow end. Thewide end is mated to the second cylindrical cavity end of separator body1702. In some embodiments, separator body 1702 is configured to operatewith the first cylindrical cavity end up. Separator body 1702 isconfigured to allow gravity to pull at least liquid and solids separatedfrom a flow of matter out collection port 1708, while gasses separatedfrom the flow of matter are pulled by suction out of suction port 1706.

Input port 1704 is configured to receive a flow of matter. In someembodiments, input port 1704 may be integral to separator body 1702.Input port 1704 may be disposed in the cylindrical cavity wall. Inputport 1704 may be located off-axis from an axis defined by thelongitudinal center of the cylindrical cavity. Input port 1704 may beconfigured to direct a flow of matter along the cylindrical cavity wall.By directing the flow of matter along the cylindrical cavity wall,liquids and gasses may cling to the wall of the cavity due to theeffects of centripetal forces. The flow of matter may be induced intoseparator system 1700 by suction received from suction port 1706 by asuction or vacuum source.

Suction port 1706 is configured to couple to a suction source. Incertain embodiments, the suction source may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 1706 to inputport 1704. Input port 1704 is configured to receive a flow of matter.The flow of matter is pulled into input port 1704 by the pressuredifference between the ambient air pressure the lower pressure providedby the suction source. The flow of matter may include liquids, solids,and gasses, including combinations thereof in varying ratios. Suctionport 1706 is disposed near the first cylindrical cavity end. Suctionport 1706 provides suction received from a suction source for operatingseparator system 1700. In some embodiments, suction port 1706 mayinclude fittings configured to attach tubing. For example, barbed orquick-disconnect type fittings may be used to couple tubing to suctionport 1706. The tubing may be used to couple suction port 1706 to asuction source or to an input port 1704 of another separator system.

Collection port 1708 is configured to expel at least liquids and solidsseparated from a flow of matter received by input port 1704. Collectionport 1708 is disposed near the narrow end of the conical cavity ofseparator body 1702. Collection port 1708 is coupled to tissue trap1762.

Baffle 1710 is disposed between input port 1704 and suction port 1706.Baffle 1710 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 1704 to suction port 1706 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 1702. In some embodiments, baffle1710 may include openings configured to allow at least gasses in a flowof matter to separate from liquids and solids that maybe included in theflow. Gasses may be pulled through baffle 1710 and out suction port1706. In an embodiment, baffle 1710 may include a solid surface locatedproximal to input port 1704. The solid surface that may be included inbaffle 1710 may be used to prevent liquids and solids in the flow frombeing pulled directly from input port 1704 to suction port 1706 byallowing time for gravity to act on the liquids and solids before theyreach an opening in baffle 1710. By allowing time for gravity to act onthe liquids and solids as they traverse the solid surface of baffle1710, the liquids and solids can descend towards collection port 1708and thereby not be suctioned out of the suction port 1706.

Vortex element 1712 is configured to direct a flow of matter in acyclonic flow. The cyclonic flow and gravity may cause liquids, solidsand gasses included in the flow of matter to separate. Vortex element1712 includes a cylindrical central member disposed within thecylindrical cavity of separator body 1702. The cylindrical centralmember forms an annular cavity between vortex element 1712 and separatorbody 1702. Vortex element 1712 is configured to allow liquids and solidsin the flow to pass through the annular cavity before dropping outcollection port 1708. In an embodiment, vortex element 1712 may includea tapered section disposed in the conical cavity of separator body 1702.In an embodiment, vortex element 1712 may include a plurality ofcylindrical sections having different diameters. The plurality ofcylindrical sections may include a first section that defines a firstportion of the annular cavity and a second section that defines a secondportion of the annular cavity. The tapered and cylindrical sections maybe configured to direct the flow within separator body 1702 in acyclonic flow pattern. In an embodiment, baffle 1710 may be integral tovortex element 1712. In an embodiment, vortex element 1712 may include alumen disposed in the cylindrical central member configured to allow atleast gasses to pass through the lumen to suction port 1706.

Collection canister 1714 is configured to receive waste from separator1702. The waste may include at least liquids and solids separated from aflow of matter received at input port 1704. Collection canister 1714 maybe used to measure the amount of liquids and/or solids separated fromthe flow of matter received at input port 1704. Collection canister 1714may be configured to permit the safe collection, transportation anddisposal of waste. In some embodiments, collection canister 1714 mayinclude a valve configured to activate when collection canister 1714 isfilled to a pre-determined volume. The valve may be used to preventwaste from leaving collection canister 1714. In some embodiments,collection canister 1714 may include a commercially available collectioncanister.

Tissue trap 1762 is configured to trap solids that may be included in acombined flow expelled from collection port 1706. Liquids included inthe combined flow are allowed to pass through tissue trap 1762 tocollection canister 1714. The solids may include tissue, blood clots,foreign objects or other solid forms of matter. Tissue trap 1762includes a means for mechanical filtration of solids that may beincluded in a combined flow expelled from collection port 1706. Solidscollected by tissue trap 1762 may be saved for analysis or safelydisposed of.

FIG. 18 is a block diagram illustrating separator with check valve 1800.In operation, separator with check valve 1800 is configured to separateliquids, solids and gasses in a flow of matter. Separator with checkvalve 1800 ejects liquids and solids separated from the flow of matterout collection port 1808 while suctioning at least gasses separated fromthe flow of matter out suction port 1806. Separator with check valve1800 is operated by suction received from a suction source. It should beunderstood that the terms “suction” and “vacuum” as used herein refer toa pressure below the surrounding ambient air pressure. Separator withcheck valve is configured to prevent a flow of matter from passingthrough suction port 1806 when check valve 1864 is activated.

In some embodiments, separator with check valve 1800 includes separatorbody 1802, input port 1804, suction port 1806, collection port 1808,baffle 1810, vortex element 1812 and check valve 1864.

Separator body 1802 includes a cylindrical wall defining a cylindricalcavity. The cylindrical wall includes a first cylindrical cavity end anda second cylindrical cavity end. Separator body 1802 also forms aconical cavity. The conical cavity has a wide end and a narrow end. Thewide end is mated to the second cylindrical cavity end of separator body1802. In some embodiments, separator body 1802 is configured to operatewith the first cylindrical cavity end up. Separator body 102 isconfigured to allow gravity to pull at least liquid and solids separatedfrom a flow of matter out collection port 1808, while gasses separatedfrom the flow of matter are pulled by suction out of suction port 1806.

Input port 1804 is configured to receive a flow of matter. In someembodiments, input port 1804 may be integral to separator body 1802.Input port 1804 may be disposed in the cylindrical cavity wall. Inputport 1804 may be located off-axis from an axis defined by thelongitudinal center of the cylindrical cavity. Input port 1804 may beconfigured to direct a flow of matter along the cylindrical cavity wall.By directing the flow of matter along the cylindrical cavity wall,liquids and gasses may cling to the wall of the cavity due to theeffects of centripetal forces. The flow of matter may be induced intoseparator with check valve 1800 by suction received from suction port1806 by a suction or vacuum source.

Suction port 1806 is configured to couple to a suction source. Incertain embodiments, the suction source may include a vacuum pump,aspirator, and/or a positive pressure operated suction source—such assuction sources that take advantage of Venturi or Coanda effect. Suctionfrom a suction source is transferred from suction port 1806 to inputport 1804. Suction port 1806 is disposed near the first cylindricalcavity end. Suction port 1806 provides suction received from a suctionsource for operating separator with check valve 1800. In someembodiments, suction port 1806 may include fittings configured to attachtubing. For example, barbed or quick-disconnect type fittings may beused to couple tubing to suction port 1806. The tubing may be used tocouple suction port 1806 to a suction source or to an input port 1804 ofanother separator.

Collection port 1808 is configured to expel at least liquids and solids.Collection port 1808 is disposed near the narrow end of the conicalcavity of separator body 1802. In an embodiment, collection port 1808may be configured to couple to a collection canister. A collectioncanister may be used to measure the matter collected from separator withcheck valve 1800. A collection canister may also be used for the safecollection, transportation and disposal of waste received from separatorwith check valve 1800. In some embodiments, collection port 1808 may becoupled to tubing or piping to direct matter to a waste drain. In someembodiments, collection port 1808 may include a mounting ring configuredto form a seal between collection port 1808 to tubing or a collectioncanister.

Baffle 1810 is configured to prevent liquids or solids in the flow frombeing pulled directly from input port 1804 to suction port 1806 withouttraversing at least a first portion of a circumference of thecylindrical wall of separator body 1802. Baffle 1810 is disposed betweeninput port 1804 and suction port 1806. In some embodiments, baffle 1810may include openings configured to allow at least gasses in a flow ofmatter to separate from liquids and solids that maybe included in theflow. Gasses may be pulled through baffle 1810 and out suction port1806. In an embodiment, baffle 1810 may include a solid surface locatedproximal to input port 1804. The solid surface that may be included inbaffle 1810 may be used to prevent liquids and solids in the flow frombeing pulled directly from input port 1804 to suction port 1806 byallowing time for gravity to act on the liquids and solids before theyreach an opening in baffle 1810. By allowing time for gravity to act onthe liquids and solids as they traverse the solid surface of baffle1810, the liquids and solids can descend towards collection port 1808and thereby not be suctioned out of the suction port 1806.

Vortex element 1812 is configured to direct a flow of matter in acyclonic flow. The cyclonic flow and gravity may cause liquids, solidsand gasses included in the flow of matter to separate. Vortex element1812 includes a cylindrical central member disposed within thecylindrical cavity of separator body 1802. The cylindrical centralmember forms an annular cavity between vortex element 1812 and separatorbody 1802. Vortex element 1812 is configured to allow liquids and solidsin the flow to pass through the annular cavity before dropping outcollection port 1808. In an embodiment, vortex element 1812 may includea tapered section disposed in the conical cavity of separator body 1802.In an embodiment, vortex element 1812 may include a plurality ofcylindrical sections having different diameters. The plurality ofcylindrical sections may include a first section that defines a firstportion of the annular cavity and a second section that defines a secondportion of the annular cavity. The tapered and cylindrical sections maybe configured to direct the flow within separator body 1802 in acyclonic flow pattern. In an embodiment, baffle 1810 may be integral tovortex element 1812. In an embodiment, vortex element 1812 may include alumen disposed in the cylindrical central member to allow at leastgasses to be pulled through the cylindrical central member and outsuction port 1806.

Check valve 1864 is configured to prevent matter from passing throughsuction port 1806 when activated. Some events that may activate checkvalve 1864 include: a collection canister filling to a predeterminedvolume, a blockage of collection port 1808, liquids flowing directlyfrom input port 1804 to suction port 1806 or some other event wherein itbecomes undesirable for matter to pass through suction port 1806. Insome embodiments, check valve 1864 may comprise a spring-operate valve.In some embodiments, check valve 1864 may include a floating member thatactivates when liquids fill separator body 1802 to a predeterminedlevel. In some embodiments, check valve 1864 may include adiaphragm-operated valve. In some embodiments, check valve 1864 mayinclude a shuttle valve.

The flow of matter may comprise a gas, a liquid, a solid, or anycombination thereof. The flow of matter may comprise one or more gases.The flow of matter may comprise one or more liquids. The flow of mattermay comprise one or more solids. The flow of matter may comprisebiological material, such as blood, extracellular fluid, lymph fluid,urine, bile, semen, fecal matter, sweat, cells, cell fragments, tissues,tissue fragments or particulates, amniotic fluid, aqueous humour,vitreous humour, bile, breast milk, cerebrospinal fluid, chyle,exudates, gastric juice, pericardial fluid, peritoneal fluid, pleuralfluid, pus, rheum, saliva, sebum, serous fluid, sputum, synovial fluid,tears, vomit, or others. The flow of matter may comprise a saltsolution, saline, an electrolyte-based fluid, sugar-containing fluids,or carbon dioxide gas. The flow of matter may comprise surgical waste,such as lavage fluids. The flow of matter may comprise gases, liquids,or solids generated from a surgical procedure.

One or more components of the system are disposable. One or moresurgical instruments, one or more flow separation devices, one or morecanisters, or any combination thereof is disposable. A surgicalinstrument is disposable. A flow separation device is disposable. Acanister is disposable.

One or more components of the system are suitable for more than a singleuse. One or more surgical instruments, one or more flow separationdevices, one or more canisters, or any combination thereof is suitablefor more than a single use. A surgical instrument is suitable for morethan a single use. A flow separation device is suitable for more than asingle use. A canister is suitable for more than a single use.

One or more components of the system are sterilized. One or moresurgical instruments, one or more flow separation devices, one or morecanisters, or any combination thereof is sterilized. A surgicalinstrument is sterilized. A flow separation device is sterilized. Acanister is sterilized.

FIG. 19 shows a separator 1902 as an element of a surgical system 1900.In some embodiments, surgical system 1900 comprises suction source 1916,tubing 1936, separator 1902, canister 1914, tubing 1930, and suctionattachment 1946.

In system 1900 a suction source 1916 applies suction to a separator 1902as described herein. The suction provided by the suction source 1916facilitates separation of a gas from a solid and/or liquid suction flowwithin the separator 1902 as described herein. In some embodiments, thegas comprises surgical smoke generated by an electrocautery instrument.In some embodiments, surgical smoke that is separated with separator1902 is evacuated into a trap. In some embodiments, surgical smoke thatis separated with separator 1902 is passed through a filter or series offilters configured to trap toxic particles and or biological elements(e.g. viruses) within the smoke. Suction attachment 1946 may comprise,for example, a suction tip such as for example, a Yankauer tip. Suctionattachment 1946 is used by a surgeon to suction material from a surgicalfield which includes, for example, blood, fat, pus, irrigation fluid,bone, surgical smoke, and other similar organic and inorganic materials.Materials suctioned from the surgical field are transmitted to theseparator 1902 through input tubing 1930. As described herein, thematerial suctioned through the surgical suction instrument is separatedin the separator 1902 so that a gas (e.g. surgical smoke) is drawn outthrough the top of the separator 1902 and any liquid and/or solidmaterial is drawn by gravity (and/or suction) into the canister 1914. Itshould be understood that while one canister and separator are shown,surgical system 1900 may also be configured for use with two or moreseparators either in series or in parallel as described herein.

A system may comprise a surgical instrument, a suction source, and oneor more separators. The one or more separators may be operativelyconnected in series, such as connected via tubing. In some cases, thesystem may also comprise collection canisters attachable to each of theone or more separators. In some cases, at least one of the one or moreseparators comprises a canister formed therein. A system comprising oneor more separators in series may permit filling a volume of a firstcanister in the series with a liquid of the flow of matter followed byfilling a volume of a second canister in the series with a liquid of theflow of matter followed by filling a volume of a third canister in theseries and so on.

A second canister may not be filled with a liquid from the flow ofmatter until at least a portion of the volume of the first canister isfilled. A third canister may not be filled with a liquid until at leasta portion of the volume of the second canister and the first canisterare filled. The portion filled with liquid may be about 70%, about 75%,about 80%, about 85%, about 90%, about 95%, about 96%, about 97%, about98%, about 99%, or 100% of the total canister volume. The portion filledwith liquid may be at least about 70% of the total canister volume. Theportion filled may be at least about 80% of the total canister volume.The portion filled may be at least about 80% of the total canistervolume. The portion filled may be at least about 90% of the totalcanister volume. The portion filled may be at least about 95% of thetotal canister volume.

When a portion of the volume of a first canister, such as about 90%, isfilled with liquid, the flow of matter may be automatically directed tothe second separator in the series to fill the second canister. When aportion of the volume of the first canister and the second canister isfilled with liquid, the flow of matter may be automatically directed tothe third separator in the series to separate gas and liquid from theflow of matter and to fill the third canister. A system of separators inseries may permit the collection of liquids from a flow of matter into aseries of canisters and separation of gas from the flow of matter duringcontinuous suction use of the surgical instrument. A system ofseparators in series permits continuous suction use of the surgicalinstrument with a greater liquid collection volume compared to a singleseparator.

FIG. 20A shows an embodiment of a separator coupled with a canister top.In the shown embodiment, the separator interface with the canister topprovides for forgoing the convergence at the bottom of the separator, sothat the separator maintains its widest diameter and empties directlyinto the canister at its widest diameter (i.e. without tapering ofseparator to form a smaller exit port). In some embodiments, thecanister top is configured to receive and couple with a wider diameterexit (i.e. opening) of a separator as shown. In some embodiments, thecanister top and the separator are fused to form one continuous piece.

FIG. 20B shows an exploded view of the separator components as describedherein. It should be understood that the embodiment of the separator andcanister top shown in FIGS. 20A and 20B are configured to be used withany and all devices, systems, and methods described herein.

In some embodiments, a flow separation device (i.e. a separator) isoperatively coupled to a canister. In some embodiments, a flowseparation device is retrofitted to an existing canister. In someembodiments, a flow separation device is integrated into a canister.

A flow separation device is operatively coupled to a surgicalinstrument. A flow separation device is operatively coupled to asurgical instrument via an input port. A flow separation device is influid communication with a surgical instrument via a tubing. A flowseparation device is attachable to a surgical instrument. A flowseparation device is retrofitted to an existing surgical instrument. Aflow separation device is an accessory, such as an optional accessory,to a surgical instrument.

In some embodiments, a flow separation device is operatively coupled toa smoke filtration canister. In some embodiments, a flow separationdevice is operatively coupled to a smoke filtration canister via a port,such as a suction port. In some embodiments, a flow separation device isin fluid 69 communication with a smoke filtration canister via a tubing.In some embodiments, a flow separation device is attachable to a smokefiltration canister. In some embodiments, a flow separation device isretrofitted to an existing smoke filtration canister. In someembodiments, a flow separation device is formed therein a smokefiltration canister. In some embodiments, a flow separation device isintegrated into a smoke filtration canister. In some embodiments, a flowseparation device is an accessory, such as an optional accessory, to asmoke filtration canister.

In some embodiments, a flow of matter enters the flow separation devicefrom the surgical instrument at the input port. The flow of matter maycomprise a gas, a liquid, a solid, or any combination thereof. The flowseparation device enhances the suction capacity of the surgicalinstrument compared to a surgical instrument without a flow separationdevice operatively coupled. The flow separation device enhances thesuction capacity of a suction source, such as a passive suction source,compared to a system without a flow separation device operativelycoupled. The flow separation device is configured to separate the gas,the liquid, the solid, or any combination thereof. The gas exits theflow separation device from a different port that the liquid exits. Forexample, the gas exits the suction port and the fluid exits thecollection port. In some embodiments, a liquid exiting the collectionport of the flow separation device is collected in a canister, such as acollection canister, that is operatively coupled to the flow separationdevice. The solid is collected in one or more filters of the flowseparation device. In some embodiments, the solid also exits thecollection port with the liquid.

The system may include one or more valves, such as a shut off valve, aball valve, a butterfly valve, a clapper valve, a check valve, a chokevalve, a diaphragm valve, a gate valve, a pinch valve, a piston valve, aplug valve, a poppet valve, a safety valve, or any combination thereof.The one or more valves is operatively coupled to the flow separationdevice, the surgical instrument, the suction source, or any combinationthereof. One or more valves are included as a safety feature of thesystem. One or more valves are included to optimize performance of thesystem. For example, a shut off valve may shut off the system if avolume of liquid within the flow separation device exceeds a specifiedvolume, such as a volume greater than 70%, 75%, 80%, 85%, 90%, 95%, 96%,97%, 98%, 99% or greater the total inner volume of the hollow body ofthe flow separation device. A shut off valve may shut off the system ifa volume of liquid within the flow separation device exceeds a volumegreater than 70% the total inner volume of the hollow body of the flowseparation device. A shut off valve may shut off the system if a volumeof liquid within the flow separation device exceeds a volume greaterthan 80% the total inner volume of the hollow body of the flowseparation device. A shut off valve may shut off the system if a volumeof liquid within the flow separation device causes the liquid to beginto exit all ports of the flow separation device.

The system may include one or more alerts. The one or more alerts areoperatively coupled to the flow separation device, the surgicalinstrument, the suction source, or any combination thereof. One or morealerts are included as a safety feature of the system. One or morealerts are included to optimize performance of the system. One or morealerts are a visual alert, an audible alert, a mechanical alert, or anycombination thereof. A visual alert is a constant light, a flashinglight, a strobing light, a light of a particular color (such asred=system off and green=system on), or any combination thereof. Anaudible alert is a ring, buzz, chime, bell, horn, vibration or otheraudible sound. An alert is a mechanical alert such as a pop-out buttonor flip tab.

FIGS. 21A, 21B, and 21C show an embodiment of the separator wherein theinput port of the separator at an angle relative to a central axis ofthe hollow body that is less than 90 degrees. In some embodiments, theinput port is angled relative to the central axis at about 85°, 80°,75°, 70°, 65°, 60°, 55°, 50°, 45°, 40°, 35°, 30°, 25°, 20° or less. Insome embodiments, the input port is angled at about 70° or less. In someembodiments, he input port is angled at about 60° or less. The inputport is angled at about 50° or less. In some embodiments, the input portis angled at about 40° or less. In some embodiments, the input port isangled at about 30° or less. In some embodiments, the input port isangled from about 20° to about 50°. In some embodiments, the input portis angled from about 40° to about 70°. In some embodiments, the inputport of the separator is angled to enhance entry of the flow of matterinto the input port, enhance a cyclonic pattern of flow along an innersurface of the hollow body, or enhance movement of liquid towards thecollection port, or any combination thereof. In some embodiments, thecyclonic pattern of flow along an inner surface of the hollow body mayaid in separation of a gas from a liquid of the flow of matter. In someembodiments, the input port of the separator is configured to direct aflow entering the separator against the wall of the separator as theflow enters the separator.

FIG. 21D shows a bottom view of an embodiment wherein an input portopening enters the separator and contacts the central column (or shaft)of the separator. Typically fluid traveling from a smaller diameterconduit into a larger diameter conduit tends to expand at the point ofintersection of the smaller conduit with the larger conduit. Here, asshown the opening of the input port enters into the larger diameterinterior of the separator so that fluid expansion is decreased (ascompared to, for example, an input port that opens directly into alarger conduit). Also shown, the opening of the input port is shaped sothat a side of the input port opening extends and contacts the centralcolumn (or shaft) while the opening gradually curves away from thatpoint so that the edge of the opening tapers away from the point atwhich the opening of the input port contacts the central column. Thisconfiguration directs flow of liquid and/solid suction material againstthe inner surface of the separator while the contact of the input portwith the column tends to draw the flow of gaseous components in thesuction flow around the central column due to a Coanda effect. Theinitial separation of the gas and fluid due to the shape and positon ofthe input port as shown in FIG. 21D enhances the separation as describedherein.

FIGS. 22A and 22B show a side view and bottom view respectively of aninput port opening into a separator wherein the opening contacts thecentral column (or shaft). Unlike the embodiment shown in FIG. 21D theopening of the input port is essentially flat without any taper. Similarto the embodiment shown in FIG. 21D, a gaseous component of a suctionflow will tend to be drawn to around the central column of the separatorwhen the suction flow enters the separator due to the Coanda effect.Because the opening of the input port opens into the separator, as inFIG. 21D, there will be a decrease or prevention of expansion of thesuction flow as it leaves the input port.

Also shown in FIGS. 21D, and 22B, a baffle comprises a solid surfacethat is proximal to the opening of the input port. Thus, openings in thebaffle do not extend around the entire circumference of the baffle. Thesolid surface of the baffle and its position immediately proximal to theopening of the input port blocks liquids and or/solids entering theseparator so that the liquids and/or solids are not immediately drawn upand out of the suction port of the separator. Rather blocking theinitial escape of solid and/or liquid components of the suction flow bythe solid portion of the baffle allows for gravity (and/or suction fromthe direction of the canister) to draw the liquids and/or solids downtowards the bottom of the separator. The gaseous components of themixture are also initially blocked by the solid component of the bafflebut these components are affected more strongly by the suction forcethrough the suction port (i.e. more strongly than gravity and/or asuction force from the direction of the canister) which draws thegaseous components up and out of the separator through the holes in thebaffle which are positioned past the solid portion of the baffle.

It should be understood that embodiments of baffles with a solid portionnear an input port may be used with any and all devices, systems, andmethods described herein.

In some embodiments, the separator comprises one or more baffles. Theone or more baffles may individually comprise a plurality of openings.The plurality of openings may comprise 3, 4, 5, 6, 7, 8, 9, 10, or moreopenings. In some embodiments, the plurality of openings is 3. In someembodiments, the plurality of openings is 4. In some embodiments, theplurality of openings is 5. In some embodiments, the plurality ofopenings is 6. In some embodiments, the plurality of openings is 7. Insome embodiments, the plurality of openings is 8. In some embodiments,the plurality of openings is 9. In some embodiments, the plurality ofopenings is 10. In some embodiments, the plurality of openings ispositioned on the one or more baffles such that they are distal to theinput port. In some embodiments, the one or more baffles is positionedon a first end of the shaft that is adjacent a second conical end. Insome embodiments, the one or more baffles are configured to receive atleast a portion of the flow of matter to pass through the one or moreopenings. In some embodiments, the one or more baffles are configured toaid in the separation of gas from liquid of the flow of matter enteringthe separator.

FIG. 23A-23D show different views of a baffle coupled with helicalsurface. In some embodiments, a baffle may be shaped or coupled with ahelix. The helix is configured to guide the flow of the liquid and/orsolid components within the suction flow along a helical track downtowards the bottom (i.e. the exit port) of the separator. A helicalbaffle may be right-handed or left-handed. The helical baffle may be aconical helix, a circular helix, a cylindrical helix, or other. Ahelical baffle may form a single complete rotation about the shaft. Ahelical baffle may form a single complete rotation about the hollowbody. A helical baffle may form more than one complete rotation aboutthe shaft. A helical baffle may form rotations along a portion of theshaft. A helical baffle may form rotations along a portion of the hollowbody. A helical baffle may form rotations about a shaft or the hollowbody along a portion of the shaft or hollow body between the suctionport and the input port.

The shaft may comprise one or more helical structures, such asindentations or protrusions. A helical structure may be right-handed orleft-handed. The helical structure may be a conic helix, a circularhelix, a cylindrical helix, or other. A helical structure may form asingle complete rotation about the shaft. A helical structure may formmore than one complete rotation about the shaft. A helical structure mayform rotations along a portion of the shaft. A helical structure mayform rotations about a shaft along a portion of the shaft between thesuction port and the input port. A helical structure may form rotationsabout a shaft along a portion of the shaft between the input port andthe collection port. A helical structure may form rotations about ashaft along the entire length of the shaft.

FIG. 24A shows an embodiment of a shaft and a baffle of a separator. Inthe shown embodiment, the shaft comprises a bulbous portion with the topmost portion shaped comprising a cone. A shaft may be integrated into aseparator or attachable thereto an inner portion of the hollow body ofthe separator.

A shaft may comprise one or more openings. An opening in a shaft maypermit one or more gases to exit the hollow body, such as via the hollowlumen of the shaft towards the suction port. An opening on the shaft maybe a circumferential gap space, such as an annular opening. An openingon the shaft may be positioned distal to the input port. An opening onthe shaft may be positioned on a portion of the bulbous end.

The shaft may be an elongate shaft. The shaft may be a cylindricalshaft. The shaft may comprise a hollow lumen. The shaft may comprise oneor more circumferential cross-section areas along the length of theshaft. Circumferential cross-section areas along the length of the shaftmay be the same. Circumferential cross-section areas along the length ofthe shaft may vary. For example, the varied circumferentialcross-section areas may form a shaft with a bulbous end, a protrudingend, a spherical end, or other. Varying the circumferentialcross-section areas along the shaft may enhance laminar flow within thehollow body, may reduce eddy currents, may prevent flow convergence, mayprevent flow divergence, or any combination thereof. For example, ashaft comprising a bulbous end positioned adjacent to a port, such as acollection port, having a circumferential cross-section area that isdifferent than the circumferential cross-section area of the hollowbody, may enhance laminar flow within the hollow body, may reduce eddycurrents, may prevent flow convergence, may prevent flow divergence, orany combination thereof.

A bulbous end of a shaft may form an initial angle of circumferentialexpansion and a secondary angle of circumferential contraction. Theinitial angle and the secondary angle may be the same. The initial angleand the secondary angle may be different.

The initial angle may be about 5 degrees, 10 degrees, 15 degrees, 20degrees, 25 degrees, 30 degrees, 35 degrees, 40 degrees, 45 degrees, 50degrees, 55 degrees, 60 degrees, 65 degrees, 70 degrees, 75 degrees, or80 degrees relative a central axis of the shaft. The initial angle maybe about 25 degrees relative a central vertical axis of the shaft. Theinitial angle may be about 30 degrees relative a central vertical axisof the shaft. The initial angle may be about 35 degrees relative acentral vertical axis of the shaft. The initial angle may be about 40degrees relative a central vertical axis of the shaft. The initial anglemay be about 40 degrees relative a central vertical axis of the shaft.

The secondary angle may be about 5 degrees, 10 degrees, 15 degrees, 20degrees, 25 degrees, 30 degrees, 35 degrees, 40 degrees, 45 degrees, 50degrees, 55 degrees, 60 degrees, 65 degrees, 70 degrees, 75 degrees, or80 degrees relative a central vertical axis of the shaft. The secondaryangle may be about 25 degrees relative a central vertical axis of theshaft. The secondary angle may be about 30 degrees relative a centralvertical axis of the shaft. The secondary angle may be about 35 degreesrelative a central vertical axis of the shaft. The secondary angle maybe about 40 degrees relative a central vertical axis of the shaft. Thesecondary angle may be about 40 degrees relative a central vertical axisof the shaft.

The separator may comprise one or more baffles within the hollow body. Abaffle may direct a flow of matter, such as a flow of matter entering aninner volume of a hollow body. In some cases, the flow of matter mayenter the inner volume via an input port. A baffle may direct a flow ofliquid entering an input port towards a collection port, such as acyclonic flow. The baffle may direct the flow of liquid away from asuction port. The baffle may encourage separation of a flow of matterinto a liquid flow stream and a gas flow stream.

A baffle may be angled relative to a central vertical axis of the shaft.A baffle may be angled at about 20 degrees, 25 degrees, 30 degrees, 35degrees, 40 degrees, 45 degrees, 50 degrees, 55 degrees, 60 degrees, 65degrees, 70 degrees, or about 75 degrees relative to a central verticalaxis of the shaft. A baffle may be angled at about 25 degrees relativeto a central vertical axis of the shaft. A baffle may be angled at about30 degrees relative to a central vertical axis of the shaft. A bafflemay be angled at about 35 degrees relative to a central vertical axis ofthe shaft. A baffle may be angled at about 40 degrees relative to acentral vertical axis of the shaft.

One or more baffles may be attachable thereto the shaft. The one or morebaffles may be formed therein the shaft. A baffle may be positionedalong the shaft at a location that is distal to the collection port andadjacent to a suction port. A baffle may be positioned along the shaftat a location that is distal to the collection port and between thesuction port and the input port. A baffle may prevent liquids enteringthe hollow body via the input port from exiting the suction port. Abaffle may be a physical barrier to prevent liquids entering the hollowbody via the input port from exiting the suction port. A baffle maydirect liquids entering the hollow body via the input port to flowtowards a collection port.

A baffle may comprise one or more openings. A baffle may be perforated.Perforations or openings in a baffle may permit one or more gases toexit the hollow body, such as via the suction port. A baffle maycomprise at least 1 opening. A baffle may comprise at least 2 openings.A baffle may comprise at least 3 openings. A baffle may comprise atleast 4 openings. A baffle may comprise at least 5 openings. A bafflemay comprise at least 6 openings. An opening on a baffle may circularshaped, rectangular shaped, oval shaped, square shaped, square shapedwith rounded edges, or others. An opening on a baffle may be acircumferential gap space, such as an annular opening. An annularopening on a baffle may be positioned adjacent to the shaft and distalfrom the outer surface of the hollow body. An opening on a baffle may bepositioned distal to the input port.

FIG. 24A-24C shows different views of embodiments of baffles includingdirection wings or fins on the openings in the baffle. In theseembodiments, the wings or fins further block fluid and/or solids in thesuction mixture from passing out through the openings in the baffle. Thewings or fins are positioned so that they are directly between thedirection of flow and the openings in the baffle and shield the openingsby both physically blocking liquid and/or solid flow into the openingsand redirecting the liquid and/or solid components downwards. In someembodiments the wings or fins have a ramp shape so that they direct theflow of a liquid and/or solid away from the opening in the baffle. Thewings or fins are configured to not block gas entry into the openings.

Example

TIME (seconds) SUCTION Yankauer (no SLS) 18 Strong Yankauer (1 SLS) 11Strong FIRST (no SLS) 133 Minimal FIRST (1 SLS) 70 Minimal FIRST (2SLS + return loop) 50 Minimal

Table 1 is a chart illustrating test results of a separator. The chartillustrates data relating to two different types of suction devices withand without a separator in use. The first type of suction device listedin the chart is a Yankauer suction tip. A Yankauer suction tip is anoral suctioning tool typically comprised of a firm plastic suction tipwith a large opening surrounded by a bulbous head and is designed toallow effective suction without damaging surrounding tissues. The secondtype of suction device (FIRST) listed in the chart is a suction devicedesigned for use in various surgical procedures and may include portsthat is variably opened and closed to adjust a ratio of liquids, solidsand gasses suctioned by the FIRST device. The term “SLS” refers to theseparator disclosed herein.

The test setup included four collection canisters coupled in series, asis used in a common operating room setup. FIG. 12 illustrates an exampleof two collection canisters 1214, 1234 including two separators 1202,1222 coupled in series. The canisters were coupled to a CONMED® System1200™ Smoke Evacuation System (SES). The chart illustrates the timetaken to suction 500 cc of 35% glycerol solution at room temperature. Inaddition, the chart illustrates data pertaining to the suction strengthof the two suction devices.

As illustrated in Table 1, the Yankauer device provided strong suctionwith and without a separator in use. However, suction time decreasedfrom 18 seconds to 11 seconds with the use of a separator system, suchas the separator examples described herein. The FIRST device was able tosuction 500 cc of 35% glycerol in 133 seconds without the use of aseparator. Adding one separator to the system decreased the suction timeto 70 seconds. Performance of the FIRST device was improved even furtherby adding a second separator to the system. The suction time of theFIRST device in conjunction with two separators decreased to 50 seconds.The data shows that the use of a separator, the examples as describedherein, may reduce the suction time of various suction times by nearlyone-half.

The foregoing description of the invention has been presented forpurposes of illustration and description. It is not intended to beexhaustive or to limit the invention to the precise form disclosed, andother modifications and variations is possible in light of the aboveteachings. The embodiment was chosen and described in order to bestexplain the principles of the invention and its practical application tothereby enable others skilled in the art to best utilize the inventionin various embodiments and various modifications as are suited to theparticular use contemplated. It is intended that the appended claims beconstrued to include other alternative embodiments of the inventionexcept insofar as limited by the prior art.

1. (canceled)
 2. A method of operating a liquid-gas flow separator,comprising: providing a cylindrical cavity having a cylindrical cavitywall, a first cylindrical cavity end, and a second cylindrical cavityend, and operating the separator with the first cylindrical cavity endbeing up; coupling a suction port to a suction source, the suction portbeing in the first cylindrical cavity end; providing a conical cavity,the conical cavity having a wide end and a narrow end, and mating thewide end to the second cylindrical cavity end; providing a collectionport at the narrow end of the conical cavity; receiving a flowcomprising a mixture of liquid and gas at a input port, the input portbeing in the cylindrical cavity wall, and inducing the flow into theseparator by the suction source, directing liquids in the flow to clingto the cylindrical cavity wall by configuring the input port; providinga baffle disposed between the input port and the suction port, therebypreventing liquids in the flow from being pulled directly from the inputport to the suction port without traversing at least a first portion ofa circumference of the cylindrical cavity wall, and allowing gasses inthe flow to separate from the liquids in the flow and pulling the gassesout of the separator via the suction port; and providing a cylindricalcentral member disposed within the cylindrical cavity, disposing thecentral member to form an annular cavity between the central member andthe cylindrical cavity wall, and passing the liquids in the flow throughthe annular cavity before dropping out the collection port.
 3. Themethod of operating a separator of claim 2, further comprising providinga flow further comprising solids and passing the solids in the flowthrough the annular cavity before dropping out the collection port. 4.The method of operating a separator of claim 2, further comprisingproviding the baffle comprising a plurality of openings to allow thegasses in the flow to be pulled out of the separator via the suctionport.
 5. The method of operating a separator of claim 2, furthercomprising preventing liquids in the flow from being pulled directlyfrom the input port to the suction port by providing the bafflecomprising a solid portion, the solid portion corresponding to at leastthe first portion of the circumference.
 6. The method of operating aseparator of claim 2, further comprising providing the central membercomprising a tapered section disposed in the conical cavity.
 7. Themethod of operating a separator of claim 2, further comprising providingthe central member comprising a plurality of cylindrical sectionscomprising different diameters.
 8. The method of operating a separatorof claim 2, further comprising providing a plurality of cylindricalsections comprising a first section defining a first portion of theannular cavity and a second section defining a second portion of theannular cavity.
 9. The method of operating a separator of claim 8,further comprising disposing the first portion between the baffle andthe second portion and disposing the second portion between the firstportion and the conical cavity.
 10. The method of operating a separatorof claim 9, further comprising providing the central member a taperedsection disposed in the conical cavity thereby forming a hollow coneshaped cavity and disposing the hollow cone shaped cavity between thesecond portion and the collection port.
 11. A method of operating aseparator in a medical environment, comprising: providing one or morefluid separators, wherein a fluid separator comprises: a cylindricalcavity comprising a cylindrical cavity wall, a first cylindrical cavityend, and a second cylindrical cavity end, the fluid separator configuredto operate with the first cylindrical cavity end being up; an suctionport operatively coupled to a suction source, the suction port being inthe first cylindrical cavity end; a conical cavity, the conical cavitycomprising a wide end and a narrow end, the wide end mated to the secondcylindrical cavity end; a collection port at the narrow end of theconical cavity; an input port to receive a flow comprising a mixture ofliquid and gas, the input port being in the cylindrical cavity wall, theflow to be induced into the separator by the suction source, the inputport configured to direct liquids in the flow to cling to thecylindrical cavity wall; a baffle disposed between the input port andthe suction port, the baffle to prevent liquids in the flow from beingpulled directly from the input port to the suction port withouttraversing at least a first portion of a circumference of thecylindrical cavity wall, the baffle to allow gasses in the flow toseparate from the liquids in the flow and be pulled out of the separatorvia the suction port; and a cylindrical central member disposed withinthe cylindrical cavity, the central member disposed to form an annularcavity between the central member and the cylindrical cavity wall, theliquids in the flow to pass through the annular cavity before droppingout the collection port; attaching the one or more separators each to anassociated waste deposit; attaching the suction port to a suctionsource; activating the suction source, thereby creating flow through theone or more separators; directing the flow using the cylindrical cavityand cylindrical central member to separate element comprising the flow;ejecting liquids and/or solids from the collection port that have beenseparated from the flow; and pulling the gas out of the suction portusing the suction source.
 12. The method of claim 11, further comprisingproviding a canister as the waste deposit.
 13. The method of claim 11,wherein attaching the suction port to a suction source comprisesattaching the suction port of a first separator to the input port of asecond separator that is attached to a suction source.
 14. The method ofclaim 11, further comprising attaching the input port of a separator toa suction device.
 15. The method of claim 14, further comprisingattaching the suction device to a surgical instrument.
 16. The method ofclaim 11, further comprising operating the one or more separators inseries by coupling the suction port of one separator to the input portof another separator, coupling the suction port of the last separator inthe series of separators to the suction source and receiving the flow atthe input of the first separator in the series of separators.
 17. Themethod of claim 16, further comprising receiving matter into the inputport of a first separator in a series of separators via the suctionsource applied to the suction port of a last separator in the series ofseparators, pulling gas out of the suction port of another separator inthe series of separators while an associated canister is filled below apre-determined capacity expelling portions of the flow out of thecollection port of another separator in the series of separators untilan associated canister is filled to a pre-determined limit.
 18. Themethod of claim 16, further comprising passing the flow, unseparated,from the input port out of the suction port of the first separator inthe series of separators when the flow is no longer ejecting from thecollection port of the first separator to the input port of anotherseparator ejecting the flow, or portions thereof, out of the collectionport.